Biosynthetic cannabinoid production methods

ABSTRACT

The present disclosure relates to the field of commercial scale production and processing of biosynthetic cannabinoids produced by growing genetically modified microalgae in a photo-bioreactor to a produce biosynthetic cannabinoids, separating a liquid nutrient medium from the genetically modified microalgae, and extracting the biosynthetic cannabinoids to produce an extracted biosynthetic cannabinoid, then distilling the extracted biosynthetic cannabinoid to produce the biosynthetic cannabinoid distillate. Biosynthetic cannabinoid distillates may be used foodstuffs, beverages, nanoemulsions, spray-dried water-soluble powders, cosmetics, or topicals.

RELATED APPLICATIONS

This application is a Continuation-In-Part of my now patented patentapplication Ser. No. 16/153,724, filed on Oct. 8, 2018, U.S. Pat. No.10,738,268, issued on Aug. 11, 2020, which is a Continuation-In-Part ofmy now patented patent application Ser. No. 15/841,886, U.S. Pat. No.10,219,536, filed on Dec. 14, 2017, and issued on Mar. 5, 2019, which isa Continuation-In-Part of my now patented patent application Ser. No.15/664,490, filed on Jul. 31, 2017, U.S. Pat. No. 10,188,086, and issuedon Jan. 29, 2019, which is a Continuation-In-Part of my now patentedpatent application Ser. No. 15/257,854, U.S. Pat. No. 10,264,769, filedon Sep. 6, 2016, and issued on Apr. 23, 2019, which is aContinuation-In-Part of my now patented patent application Ser. No.15/242,579, U.S. Pat. No. 10,188,083, filed on Aug. 21, 2016, and issuedon Jan. 29, 2019. The contents of the aforementioned applications areincorporated by reference in their entirety.

TECHNICAL FIELD

The present disclosure relates to the field of commercial scaleproduction and processing of insects, cannabis, and biosyntheticcannabinoids to produce foodstuffs, consumer products, emulsions, drugs,pharmaceutical compositions, beverages, crystals, powders, softgels,surfactants, and oils, for medicinal or recreational, biotechnology,medical, and agrochemical applications.

BACKGROUND

Efficient, reliable, and consistent computer operated insect rearingfacilities are needed to meet the insect production demands of society.In recent years, there has been an increasing demand for insect proteinfor human and animal consumption. There is also promise for theextraction and use of lipids from insects for applications involvingmedicine, nanotechnology, consumer products, and chemical production.Large scale insect production systems must be designed responsibly tomake sure that the insects are freed from hunger, thirst, discomfort,pain, injury, disease, fear and distress. These systems must beprecisely sized and situated to be able to provide systematically timedand controlled computer operated methods to maintain a sufficient amountof nutrition, to prevent disease, cannibalism, and injury. A need existsfor mass insect production facilities that maximize insect production ona small physical outlay while providing adequate space for high densityinsect rearing.

The ability to grow insects with minimal human interaction has been longregarded as desirable or needed to facilitate widespread use for humanand animal or consumption or for use as an intermediate lipid-basedproduct for the production of food and chemicals. In coming years,nuclear proliferation, food shortages, water scarcity, and diminishingpetroleum reserves may result in a constraint on access to food, water,chemicals, and other resources. Famine may result causing millions ofdeaths over an extended number of years which will mark a clear end tothe period of growth and prosperity for the human civilization,industrialization, and globalization.

Thus, it is of paramount importance that large-scale, modular, easilymanufacturable, energy efficient, reliable, computer operated insectproduction facilities are extensively deployed to produce insects forhuman and animal consumption, and for the extraction and use of lipidsfor applications involving medicine, nanotechnology, consumer products,and chemical production with minimal water, feedstock, and environmentalimpact.

There is a need for systems and methods that can clean and decontaminatewater from the most-harshest of environmental conditions and provide aclean water source suitable to feed and grow insects for human, animal,and chemical production. There is a need to develop and vastly implementlarge-scale, systematic insect feeding and breeding facilities that canaccommodate the protein and fatty acid demands of society. There is aneed to re-use old containerized shipping containers to promote theimplementation of widespread commercial production of insects to promoteregional, rural, and urban, job opportunities that maximizes the qualityof living the insects that are farmed.

A need exists for cannabis farming facilities that maximize plantproduction on a small physical outlay while providing adequate space forhigh-density plant growth all at an economically attractive cost. Thereis a need for systems and methods that can produce unique and novelfoodstuffs or snack foods. There is a need for unique and novelfoodstuffs or snack foods to be created from Orthoptera order of insectsand produced from commercially available unit operations, including,feedstock mixing, enhanced feedstock splitting, insect feeding, insectbreeding, insect collection, insect grinding, pathogen removal,multifunctional composition mixing, liquid mixing, shaping, cooking,flavoring, biocatalyst mixing, exoskeleton separation, liquidseparation, and lipid extraction.

There is a need to make electrochemical biosensors made from insects formedicinal, environmental, agricultural, and food-related industrialmarket sectors. There is a need for insect pest management systems forcannabis farms. There is a need for an insect traceability system thatis specifically tailored towards the unique challenges related totracking, accountability, food safety, and state and federal governmentcompliance of the insect industry, either for food (for humans oranimals), drugs, chemicals, and medicine.

There is a need for systems to hydrogenate insect oil. There is a needfor systems to produce distilled and purified insect oils There is aneed for systems to esterify hydrogenated insect oil to makeintermediate products for the production of consumer products including,baby lotion, biomedical sensing device, blush, body cream, candles,cleanser, cologne, concealer, food, foot powder, foot spray, foundation,hand cream, hard candy, lubricant, mascara, moisturizer, nail products,nano-device, oils, perfume, pharmaceuticals, powders, shaving cream,soap, surfactant, thickeners. There is a need for systems to processinsect oil to produce intermediate products from stearic acid theintermediate product includes one or more intermediate products selectedfrom the group consisting of glyceryl stearate, TEA-stearate, sorbitanstearate, and stearyl alcohol. There is a need to saponify insect oil toproduce surfactants. There is a need to produce pharmaceuticalcompositions, including a cannabinoid, a recombinant protein, vaccine,antibody, peptide, or chemical and various other therapeutics andcosmetic personal products from insects using high-tech advancements inbioprocessing, chemical, and controls, and automation engineeringtechnologies.

Efficient, reliable, and consistent, computer-operated cannabis farmingsystems and methods are needed to meet the cannabis production demandsof society. In recent years, there has been an increasing demand forcannabis for medicinal and recreational use. Large-scale cannabisfarming systems must be designed carefully to minimize environmentalimpact, reduce manual labor and human interaction, and automate thesystem as much as possible while maximizing plant growth. These systemsmust be precisely sized and situated to be able to providesystematically timed and controlled computer-operated methods tomaintain a sufficient amount of water and nutrients for the cannabis ata precise temperature, humidity level, pH, oxygen and/or carbon dioxidelevel, air velocity, and light wavelength and schedule.

A need exists for an insect farm co-located at a cannabis farm topurposefully introduce insects into the cannabis plants to protect theplants allowing the insects to feed on other insect eggs, insect larva,and other insects including living organisms which may or may notcontain chitin not only including spider mites, rust mites, thrips,jumping plant lice, white fly, knats, gnats, aphids, and insects. Thereis a need for computer-operated bat farms to protect cannabis plantswithin cannabis farms by purposefully introducing bats to the cannabisfarm to feed on insects.

The ability to grow cannabis with minimal human interaction has beenlong regarded as desirable and needed to facilitate widespread use forhuman consumption and for the production of food. It is of importancethat large-scale, standardized, modular, easily manufacturable, energyefficient, reliable, computer-operated cannabis farming systems andfacilities are extensively deployed to produce cannabis for medicinaland recreation use with minimal water and environmental impact.

A need exists for an insect farm co-located at a mushroom farm topurposefully introduce insects into the mushroom plants to protect theplants allowing the insects to feed on other insect eggs, insect larva,and other insects including living organisms which may or may notcontain chitin not only including spider mites, rust mites, thrips,jumping plant lice, white fly, knats, gnats, aphids, and insects. Thereis a need for computer-operated bat farms to protect mushroom plantswithin mushroom farms by purposefully introducing bats to the mushroomfarm to feed on insects.

The ability to grow mushroom with minimal human interaction has beenlong regarded as desirable and needed to facilitate widespread use forhuman consumption and for the production of food. It is of importancethat large-scale, standardized, modular, easily manufacturable, energyefficient, reliable, computer-operated mushroom farming systems andfacilities are extensively deployed to produce mushroom for medicinaland recreation use with minimal water and environmental impact.

There is a need for cannabis farming facilities to employ systems andmethods that can clean and decontaminate water from harsh andunpredictable sources and provide a clean water source suitable to feedand grow cannabis. There is a need to re-use old containerized shippingcontainers to promote the implementation of widespread commercialproduction of cannabis to promote regional, rural, and urban jobopportunities that maximize the quality of living where the cannabis isfarmed.

There is a need for a superior blend of Cannabis sativa L. ssp. Sativaand Cannabis sativa L. ssp. Indica (Lam.) that provides improvedmedicinal benefits, and has a high yield to meet industrial, commercial,recreational, and medicinal demand at a low price and minimal economicand environmental impact. There is a need for a new variety of plantthat has a repeatable, predictable, and unique chemical composition thatis based upon standardized engineered concentrations of: cannabidiol,tetrahydrocannabinol, energy, carbon, oxygen, hydrogen, ash, volatiles,nitrogen, sulfur, chlorine, sodium, potassium, iron, magnesium,phosphorous, calcium, zinc, cellulose, lignin, hemicellulose, fat,fiber, protein, while having preferred specific Cannabis sativa L. ssp.Sativa and Cannabis sativa L. ssp. Indica (Lam.) weight percentages.

SUMMARY

This Summary is provided merely to introduce certain concepts and not toidentify any key or essential features of the claimed subject matter.

Paragraph A. A method to produce a biosynthetic cannabinoid distillate,the method includes:

-   (a) in a photo-bioreactor, growing microalgae which have been    genetically modified to produce a biosynthetic cannabinoid, in a    liquid nutrient medium;-   (b) separating the grown, genetically modified microalgae from the    liquid nutrient medium;-   (c) extracting the biosynthetic cannabinoid from the grown,    genetically modified microalgae to produce an extracted biosynthetic    cannabinoid; and-   (d) distilling the extracted biosynthetic cannabinoid to produce the    biosynthetic cannabinoid distillate.    Paragraph B. The method according to Paragraph A, comprising:    (e) producing a beverage from the biosynthetic cannabinoid    distillate.    Paragraph C. The method according to Paragraph A, wherein:    (e) producing a nanoemulsion from the biosynthetic cannabinoid    distillate.    Paragraph D. The method according to Paragraph C, wherein:    (f) spray drying the nanoemulsion to produce a spray-dried    water-soluble powder.    Paragraph E. The method according to Paragraph A, comprising:    (e) mixing the biosynthetic cannabinoid distillate with cannabis    plant derived terpenes.    Paragraph F. The method according to Paragraph A, comprising:    (e) mixing the biosynthetic cannabinoid distillate with    non-biosynthetic plant derived cannabinoids.    Paragraph G. The method according to Paragraph A, comprising:    (e) producing a foodstuff from the biosynthetic cannabinoid    distillate, the foodstuff includes one or more selected from the    group consisting of ada, bagels, baked goods, beverages, biscuits,    bitterballen, bonda, breads, cakes, candies, cereals, chips,    chocolate bars, carbonated soft drinks, carbonated drinks,    chocolate, coffee, cokodok, confectionery, cookies, cooking batter,    corn starch mixtures, crackers, crêpes, croissants, croquettes,    croutons, dolma, dough, doughnuts, energy bars, flapjacks, french    fries, frozen custard, frozen desserts, frying cakes, fudge, gelatin    mixes, granola bars, gulha, hardtack, ice cream, khandvi, khanom    buang, krumpets, meze, mixed flours, muffins, multi-grain snacks,    nachos, nian gao, noodles, nougat, onion rings, pakora, pancakes,    panforte, pastas, pastries, pie crust, pita chips, pizza,    poffertjes, pretzels, protein powders, pudding, rice krispie treats,    sesame sticks, smoothies, snacks, soft drinks, sport drinks,    sparkling drinks, specialty milk, tele-bhaja, tempura, toffee,    tortillas, totopo, turkish delights, or waffles.    Paragraph H. The method according to Paragraph A, comprising:    (f) producing a cosmetic product or a topical from the biosynthetic    cannabinoid distillate.    Paragraph I. The method according to Paragraph A, wherein:-   the liquid nutrient medium includes treated water, the treated water    is treated with an adsorbent, ion exchange resin, a membrane, and/or    an ultraviolet unit.    Paragraph J. The method according to Paragraph A, wherein:    in step (a), introducing a gas to the liquid nutrient medium, the    gas includes carbon dioxide.    Paragraph K. The method according to Paragraph J, wherein:    the photo-bioreactor includes a superficial gas velocity ranging    from between 0.1 to 15 inches per second.    Paragraph L. T The method according to Paragraph A, wherein:    in step (a), the liquid nutrient medium includes one or more    selected from the group consisting of a carbohydrate, a    micronutrient, a macronutrient, an acid, and combinations thereof.    Paragraph M. The method according to Paragraph A, wherein: The    method according to claim 1, wherein:    in step (a), growing the genetically modified microalgae within a    photo-bioreactor at a residence time ranging from 1 to 5 days.    Paragraph NM. The method according to Paragraph A, wherein:    in step (a), the photo-bioreactor operates at a photosynthetic    photon flux density ranging from ranging from 50 to 1,000 micromole    per second and square meter.    Paragraph O. The method according to Paragraph A, wherein:    in step (a), the photo-bioreactor is provided with a photon flux    density source including one or more selected from the group    consisting of compact fluorescent lights, incandescent lights,    fluorescent lights, halogen lights, metal halide lamps,    high-intensity discharge gas discharge lamps, low pressure sodium    lamps, sodium lamps, quartz halogen lamps, and combinations thereof.    Paragraph P. The method according to Paragraph A wherein:    in step (a), the photo-bioreactor is provided with a photon flux    density source light emitting diodes, wherein the light emitting    diodes operate at a wave length ranging from 390 to 700 nanometers.    Paragraph Q. T The method according to Paragraph A, wherein:    in step (a), the photo-bioreactor is transparent and/or translucent.    Paragraph R. The method according to Paragraph A, wherein:    in step (a), the photo-bioreactor has a volume ranging from 50 to    2000 liters.    Paragraph S. The method according to Paragraph A, wherein:    in step (d), distilling the extracted biosynthetic cannabinoid via    spinning band distillation.    Paragraph T. A method to produce an extracted biosynthetic    cannabinoid, the method includes:-   (a) in a photo-bioreactor, growing microalgae and/or cyanobacterium    which have been genetically modified to produce a biosynthetic    cannabinoid, in a liquid nutrient medium and in the presence of    carbon dioxide, the liquid nutrient medium including water treated    with an adsorbent, ion exchange resin, and/or a membrane;-   (b) separating the grown, genetically modified microalgae and/or the    genetically modified cyanobacterium from the liquid nutrient medium;    and-   (c) extracting the biosynthetic cannabinoid from the grown,    genetically modified microalgae and/or the genetically modified    cyanobacterium to produce an extracted biosynthetic cannabinoid.    Volume I: Insect Production Superstructure System (IPSS),    Description of the Drawings

Reference will now be made in detail to various embodiments of thedisclosure. Each embodiment is provided by way of explanation of thedisclosure, not limitation of the disclosure. In fact, it will beapparent to those skilled in the art that modifications and variationscan be made in the disclosure without departing from the teaching andscope thereof. For instance, features illustrated or described as partof one embodiment to yield a still further embodiment derived from theteaching of the disclosure. Thus, it is intended that the disclosure orcontent of the claims cover such derivative modifications and variationsto come within the scope of the disclosure or claimed embodimentsdescribed herein and their equivalents.

Additional objects and advantages of the disclosure will be set forth inpart in the description which follows, and in part will be obvious fromthe description, or may be learned by practice of the claims. Theobjects and advantages of the disclosure will be attained by means ofthe instrumentalities and combinations and variations particularlypointed out in the appended claims.

The accompanying figures show schematic process flowcharts of preferredembodiments and variations thereof. A full and enabling disclosure ofthe content of the accompanying claims, including the best mode thereofto one of ordinary skill in the art, is set forth more particularly inthe remainder of the specification, including reference to theaccompanying figures showing how the preferred embodiments and othernon-limiting variations of other embodiments described herein may becarried out in practice, in which:

FIG. 1A shows a simplistic block flow diagram of one embodiment of anInsect Production Superstructure System (IPSS) including the sequencesteps of feedstock mixing (step A), feedstock splitting (step B), insectfeeding (step C1, C2), insect breeding (step D), insect collection (stepE), and insect grinding (step F).

FIG. 1B elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence steps of pathogen removal (step G) andmultifunctional composition mixing (step H).

FIG. 1C elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence step of lipid extraction (step J).

FIG. 1D includes one non-limiting embodiment of an insect traceabilitysystem flow chart.

FIG. 2 shows a non-limiting embodiment of an enhanced feedstock mixingmodule (1000) including a feedstock distribution module (1A), mineraldistribution module (1B), vitamin distribution module (1C), polymerdistribution module (1D), water distribution module (1E), and anenhanced feedstock distribution module (1F).

FIG. 3 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein the egg transfer system (244) of theinsect feeding module (2000) is at a first state in a first retractedheight (H1).

FIG. 4 shows one non-limiting embodiment of a network (220) of cells(219) for growing insects within a feeding chamber (200) of the insectfeeding module (2000) shown in FIG. 3.

FIG. 5 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a second mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a second state at a second elevated height (H2) so as topermit insects (225) to lay eggs (259) within a provided breedingmaterial (248).

FIG. 6 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a third mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a first state in a first retracted height (H1) so as todiscontinue insects (225) from laying eggs (259) within the providedbreeding material (248).

FIG. 7 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) and insect evacuation module (3000)operating in a fourth mode of operation wherein a vibration unit (214)is activated to permit the removal of insects (225) from the network(220) of cells (219) and wherein the insect evacuation module (3000)separates insects from gas while a vacuum is pulled on the insectfeeding module (2000) via an insect evacuation fan (312)

FIG. 8 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein a plurality of slats (341) of an eggtransfer system (244) of the insect feeding module (2000) are in firstclosed state (341A).

FIG. 9 elaborates upon the non-limiting embodiment of FIG. 8 and showsbreeding material (248) resting upon the surface of the plurality ofslats (341) of the egg transfer system (244) so as to permit insects(225) to lay eggs (259) within the breeding material (248).

FIG. 10 elaborates upon the non-limiting embodiment FIG. 8 but shows theegg transfer system (244) in a second open state (341A) so as to permitegg-laden breeding material (248) to pass through the plurality of slats(341) while the vibration unit (214) is activated, some insects (225)may pass through the open slats (341) as well.

FIG. 11 shows a simplistic diagram illustrating an insect grindingmodule that is configured to grind at least a portion of the insectstransferred from the insect evacuation module (3000).

FIG. 12A shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000) by useof at least one solvent.

FIG. 12B shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000) byusing of no solvent by way of an expeller press.

FIG. 12C shows one non-limiting embodiment of a hydrogenation system(12C) configured to hydrogenate the insect lipids (1518, 1552) toproduce hydrogenation insect lipids (12CC).

FIG. 12D shows one non-limiting embodiment of an esterification system(12D) configured to produce esterified insect lipids.

FIG. 13 shows a simplistic diagram illustrating a pathogen removalmodule that is configured to remove pathogens from at least a portion ofthe insects transferred from the insect evacuation module (3000).

FIG. 14A shows a simplistic diagram illustrating a multifunctionalcomposition mixing module that is configured to generate amultifunctional composition from at least a portion of the insectstransferred from the pathogen removal module and including the sequencesteps or sub-modules including an insect distribution module (6A),fiber-starch distribution module (6B), binding agent distribution module(6C), density improving textural supplement distribution module (6D),moisture improving textural supplement distribution module (6E),multifunctional composition mixing module (6F).

FIG. 14B shows a simplistic diagram illustrating a multifunctionalcomposition mixing module that is configured to generate amultifunctional composition as described in FIG. 14A however insteadfrom at least a portion of the insects transferred from the insectgrinding module.

FIG. 14C shows one non-limiting embodiment of a liquid mixing module(LMM) that is configured to mix water with multifunctional composition(6F23) provided from the multifunctional composition mixing module asshown in FIG. 14A or 14B.

FIG. 14D shows one non-limiting embodiment of a shaping module (14D)that is configured to shape the multifunctional composition and watermixture (C17) to produce a shaped multifunctional composition mixture(D10).

FIG. 14E shows one non-limiting embodiment of a cooking module (14E)that is configured to cook the shaped multifunctional compositionmixture (D10) provided from the shaping module (14D) to form a cookedmultifunctional composition mixture (E18A).

FIG. 14F shows one non-limiting embodiment of a flavoring module (14F)that is configured to flavor the cooked multifunctional compositionmixture (E18A) provided from the cooking module (14E) to form a flavoredmultifunctional composition mixture (F10).

FIG. 14G shows one non-limiting embodiment of a biocatalyst mixingmodule (14G) that is configured to mix insects, water, biocatalyst, andoptionally acid to create an insect liquid biocatalyst mixture (G09).

FIG. 14H shows one non-limiting embodiment of an exoskeleton separationmodule (14H) that is configured to remove the exoskeleton containedwithin the insect liquid biocatalyst mixture (G09). FIG. 14I shows onenon-limiting embodiment of a liquid separation module (LSM) that isconfigured to remove liquid from the exoskeleton-depleted insect liquidmixture (H39) to provide an insect-depleted liquid mixture (I19) andinsects (I46).

FIG. 14J shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to produce a vaporized liquid (J22) and astream of liquid-depleted insects (J10).

FIG. 14K shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from an insect liquid mixture(H39) by use of a spray dryer (KAP).

FIG. 14K-1 shows one non-limiting embodiment of a co-current type ofspray dryer (KAP) that may be used with the liquid separation module(LSM) described in FIG. 14K.

FIG. 14K-2 shows one non-limiting embodiment of a counter-current typeof spray dryer (KAP) that may be used with the liquid separation module(LSM) described in FIG. 14K.

FIG. 14K-3 shows another non-limiting embodiment of a counter-currenttype of spray dryer (KAP) that may be used with the liquid separationmodule (LSM) described in FIG. 14K.

FIG. 14K-4 shows a non-limiting embodiment of a mixed-flow type of spraydryer (KAP) that may be used with the liquid separation module (LSM)described in FIG. 14K.

FIG. 14KK shows one non-limiting embodiment of aninsect-derived-biosensor including a transducer and aninsect-derived-biopolymer.

FIG. 14L shows a power production system (PPS) that is configured togenerate electricity, heat, or steam for use in the Insect ProductionSuperstructure System (IPSS).

FIG. 15 shows a simplistic diagram illustrating a plurality of feedingchambers (FC1, FC2, FC3) of an insect feeding module (2000) integratedwithin one common separator (300) of an insect evacuation module (3000).

FIG. 16 shows a simplistic diagram illustrating a plurality ofseparators (S1, S2, S3) integrated with one common feeding chamber(FC1), and wherein the feeding chamber (FC1) and second separator (S2)are in fluid communication with one common breeding chamber (BC), andwherein the breeding chamber (BC) is in fluid communication with onecommon breeding material and insect separator (SEPIA), and wherein thebreeding material and insect separator (SEPIA) is in fluid communicationwith at least one of a plurality of feeding chambers (FC1, FC2, FC3).

FIG. 16A shown one embodiment of a plurality of separators (KGA, KGB,KGC) that are configured to pull a vacuum on a plurality of insectfeeding chambers (FC1, FC2, FC3) and separate large insects (KGG), smallinsects (KGH), and particulates (KGI) therefrom while returning thesmall insects (KGH) back to the plurality of insect feeding chambers(FC1, FC2, FC3).

FIG. 17 shows a perspective view of one embodiment of a scalableportable modular Insect Production Superstructure System (IPSS) designedwith: one enhanced feedstock mixing module (1000); three insect feedingmodules (2000A, 2000B, 2000C); one insect evacuation module (3000);three insect breeding modules (4000A, 4000B, 4000C), and three insectseparation modules (5000).

FIG. 18 shows a front view of one embodiment of an enhanced feedstockmixing module (1000) module including a feedstock distribution module(1A), mineral distribution module (1B), vitamin distribution module(1C), and a polymer distribution module (1D).

FIG. 19 shows a top view of one embodiment of an enhanced feedstockmixing module (1000) including a feedstock distribution module (1A),mineral distribution module (1B), vitamin distribution module (1C), anda polymer distribution module (1D).

FIG. 20 shows a first side view of one embodiment of an enhancedfeedstock mixing module (1000).

FIG. 21 shows a front view of one embodiment of a water distributionmodule (1E).

FIG. 22 shows a top view of one embodiment of a water distributionmodule (1E).

FIG. 23 shows a first side view of one embodiment of a waterdistribution module (1E).

FIG. 24 shows a front view of one embodiment of an enhanced feedstockdistribution module (1F).

FIG. 25 shows a top view of one embodiment of an enhanced feedstockdistribution module (1F).

FIG. 26 shows a first side view of one embodiment of an enhancedfeedstock distribution module (1F).

FIG. 27A shows a front view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C).

FIG. 28A shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C).

FIG. 27B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 27C shows a top view of one embodiment of an insect feeding module(2000, 24000A, 2000B, 2000C) equipped with a humidity control unit(HCU).

FIG. 27D shows one non-limiting embodiment where the compressor (Q30)within the humidity control unit (HCU) is that of a thermal compressor(Q30) that accepts a source of steam.

FIG. 27E shows one non-limiting embodiment where the compressor (Q30)within the humidity control unit (HCU) is that of a thermal compressor(Q30) that accepts a source of steam.

FIG. 27F elaborates upon FIG. 27E and shows one non-limiting embodimentwhere the compressor (Q30) within the humidity control unit (HCU) isthat of a thermal compressor (Q30) that accepts a source of heat, suchas flue gas (FG1).

FIG. 28B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 29 shows a first side view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C).

FIG. 30 shows a front view of one embodiment of an insect evacuationmodule (3000).

FIG. 31 shows a top view of one embodiment of an insect evacuationmodule (3000).

FIG. 32 shows a first side view of one embodiment of an insectevacuation module (3000).

FIG. 33 shows a front view of one embodiment of an insect breedingmodule (4000, 4000A).

FIG. 34 shows a top view of one embodiment of an insect breeding module(4000, 4000A).

FIG. 34A shows a top view of one embodiment of an insect breeding module(4000, 4000A, 4000B, 4000C) equipped with a humidity control unit (HCU).

FIG. 34B shows one non-limiting embodiment where the compressor (QQ30)within the humidity control unit (HCU) is that of a thermal compressor(QQ30) that accepts a source of steam.

FIG. 35 shows a first side view of one embodiment of an insect breedingmodule (4000, 4000A) at a cutaway section of the conveyor side view(CSV).

FIG. 36 shows a second side view of one embodiment of an insect breedingmodule (4000, 4000A) at a cutaway section of the conveyor side view(CSV).

FIG. 37 shows a front view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 38 shows a top view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 39 shows a first side view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 40A shows Table 1 with upper and lower ranges of feedstock mineralenhancers, feedstock vitamin enhancers, feedstock polymer enhancers, andother ‘energy-Insect®’ enhancers.

FIG. 40B shows one non-limiting example of process conditions within anInsect Production Superstructure System (IPSS).

FIG. 40C shows nutritional requirements of insects produced in an InsectProduction Superstructure System (IPSS) that are fed an enhancedfeedstock.

FIG. 41A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 41B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 42A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 42B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 43A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 43B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 44A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects.

FIG. 44B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects.

FIG. 45A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects to generate a multifunctional composition.

FIG. 45B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional composition.

FIG. 46 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional composition.

FIG. 47 shows one non-limiting embodiment of a method for raisingOrthoptera order of insects for the separation of lipids containedwithin said insects.

FIG. 48 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects for the extraction of lipids FIG. 1A′depicts one non-limiting embodiment of a farming superstructure system(FSS) including a first water treatment unit (A1*), a second watertreatment unit (A2*), a third water treatment unit (A3*), a commonreservoir (500*), a pump (P1*), a plurality of vertically stackedgrowing assemblies (100*, 200*), a fabric (104*, 204*) that partitionseach growing assembly (100*, 200*) into an upper-section (105*, 205*)and a lower-section (106*, 206*), a plurality of lights (L1*, L2*)positioned within the upper-section (105*, 205*) of each growingassembly.

FIG. 1B′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) that includes a first growing assembly (100*) having afirst growing medium (GM1*) and a second growing assembly (200*) havinga second growing medium (GM2*).

FIG. 1C′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) that includes a first growing assembly (100*) having afirst growing medium (GM1*) and a second growing assembly (200*) havinga second growing medium (GM2*) and the first growing assembly (100*) andsecond growing assembly (200*) are grown outdoors.

FIG. 1D′ depicts one non-limiting embodiment general arrangement of afarming superstructure system (FSS) top-view that includes a firstgrowing assembly (100*) and a second growing assembly (200*) eachconfigured to grow plants (107*, 107A*, 107B*, 107C*, 20*7, 207A*,207B*, 207C*).

FIG. 2′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) including a first vertically stacked system (1500*)including a plurality of vertically stacked growing assemblies (100*,200*) integrated with a first and second vertical support structure(VSS1*, VSS2*) wherein the first growing assembly (100*) is supported bya first horizontal support structure (SS1*) and a second growingassembly (200*) is supported by a second horizontal support structure(SS2*).

FIG. 3′ depicts one non-limiting embodiment of a plurality of verticallystacked systems (1500*, 1500′*) including a first vertically stackedsystem (1500*) and a second vertically stacked system (1500′*), thefirst vertically stacked system (1500*) as depicted in FIG. 2′, alsoboth vertically stacked systems (1500*, 1500′*) are contained within anenclosure (ENC*) having an interior (ENC1*).

FIG. 4A′ depicts one non-limiting embodiment of FIG. 3′ wherein theenclosure (ENC*) is provided with a temperature control unit (TCU*)including an air heat exchanger (HXA*) that is configured to provide atemperature and/or humidity controlled air supply (Q3*) to the interior(ENC1*) of the enclosure (ENC*) which contains a plurality of verticallystacked systems (1500*, 1500′*).

FIG. 4B′ depicts one non-limiting embodiment of FIG. 1B′ and FIG. 4A′wherein the enclosure (ENC*) is provided with a temperature control unit(TCU*) including an air heat exchanger (HXA*) that is configured toprovide a temperature and/or humidity controlled air supply (Q3*) to theinterior (ENC1*) of the enclosure (ENC*) which contains a plurality ofgrowing assemblies (100*, 200*).

FIG. 5A′ depicts one non-limiting embodiment of FIG. 4A′ wherein thetemperature control unit (TCU*) of FIG. 4A′ is contained within theinterior (ENC1*) of the enclosure (ENC*) and coupled with a humiditycontrol unit (HCU*).

FIG. 5B′ depicts one non-limiting embodiment of FIG. 4B′ and FIG. 5A′wherein the temperature control unit (TCU*) of FIG. 4B′ is containedwithin the interior (ENC1*) of the enclosure (ENC*) and coupled with ahumidity control unit (HCU*).

FIG. 5C′ shows one non-limiting embodiment where the compressor (Q30*)within the humidity control unit (HCU*) is that of a thermal compressor(Q30*) that accepts a source of steam.

FIG. 5D′ shows one non-limiting embodiment where the compressor (Q30*)within the humidity control unit (HCU*) is that of a thermal compressor(Q30*) that accepts a source of steam.

FIG. 5E′ elaborates upon FIG. 5D′ and shows one non-limiting embodimentwhere the compressor (Q30*) within the humidity control unit (HCU*) isthat of a thermal compressor (Q30*) that accepts a source of heat, suchas flue gas (FG1*)

FIG. 6′ shows a front view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

FIG. 7′ shows a top view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

FIG. 8′ shows a first side view of one embodiment of a plant growingmodule (PGM*).

FIG. 9′ shows a front view of one embodiment of a liquid distributionmodule (LDM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications andthat is configured to provide a source of liquid to a plurality of plantgrowing modules (PGM*).

FIG. 10′ shows a top view of one embodiment of a liquid distributionmodule (LDM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications andthat is configured to provide a source of liquid to a plurality of plantgrowing modules (PGM*).

FIG. 11′ shows a first side view of one embodiment of a liquiddistribution module (LDM*).

FIG. 12′ shows one non-limiting embodiment of a fabric (104*) used in agrowing assembly (100), the fabric (104) having a multi-pointtemperature sensor (MPT10*0) connected thereto for measuringtemperatures at various lengths along the sensor's length.

FIG. 13′ shows another one non-limiting embodiment of a fabric (104*)used in a growing assembly (100).

FIG. 14′ depicts a computer (COMP) that is configured to input andoutput signals listed in FIGS. 1-17K′.

FIG. 15′ shows a plurality of cannabis trimmers (TR*, TR**) that areconfigured to trim at least a portion of the cannabis (107*, 207*) thatwas growing in each growing assembly (100*, 200*).

FIG. 16′ shows a grinder (GR*) that is configured to grind at least aportion of cannabis plants (107, 207*) that was growing in each growingassembly (100*, 200*).

FIG. 17′ shows a heater (HTR1*) that is configured to heat at least aportion of cannabis plants (107*, 207*) that was growing in each growingassembly (100*, 200*).

FIG. 17A′ shows one non-limiting embodiment of a volatiles extractionsystem (VES*) that is configured to extract volatiles from cannabis(107*, 207*) with a first solvent (SOLV1*).

FIG. 17A″ shows one non-limiting embodiment of a volatiles extractionsystem (VES*) that is configured to extract volatiles from cannabis(107*, 207*) with a chilled ethanol separation system (CESS).

FIG. 17B′ shows a plurality of volatiles extraction systems (VES1*,VES2*) equipped with one first solvent separation system (SSS*).

FIG. 17C′ shows a volatiles and solvent mixing system (VSMS*) that isconfigured to mix the volatiles (VOLT*) with a second solvent (SOLV2*).

FIG. 17D′ shows a separation system (SEPSOL*)separation system (SEPSOL*)that is configured to separate at least a portion of the solvent(SOLV2*) from the volatiles and solvent mixture (SVSM*) to produceconcentrated volatiles (CVOLT*).

FIG. 17D″ shows a plurality of sequential separation systems (SEPSOL*,SEPSOL**, SEPSOL***) that are configured to separate at least a portionof the solvent, volatiles, and/or cannabinoids from produce concentratedvolatiles (CVOLT*) and a plurality of different compounds (1SCM*,1SCM**, 2SCM*, 2SCM**)

FIG. 17E′ shows one non-limiting embodiment of a solvent separationsystem that is configured to evaporator the second solvent from thevolatiles and solvent mixture (SVSM*) by use of a spray dryer (KAP*).

FIG. 17E-1′ shows one non-limiting embodiment of a co-current type ofspray dryer (KAP*) that may be used with the solvent separation systemdescribed in FIG. 17E′.

FIG. 17E-2′ shows one non-limiting embodiment of a counter-current typeof spray dryer (KAP*) that may be used with the solvent separationsystem described in FIG. 17E′.

FIG. 17E-3′ shows another non-limiting embodiment of a counter-currenttype of spray dryer (KAP*) that may be used with the solvent separationsystem described in FIG. 17E′.

FIG. 17E-4′ shows one non-limiting embodiment of a mixed-flow type ofspray dryer (KAP*) that may be used with the solvent separation systemdescribed in FIG. 17E′.

FIG. 17F′ shows a power production system (PPS*) that is configured togenerate electricity, heat, or steam for use in the farmingsuperstructure system (FSS).

FIG. 17G′ shows one non-limiting embodiment of a carbon dioxide removalsystem (GAE*) that is configured to remove carbon dioxide from flue gas(LFP*) for use as a source of carbon dioxide (CO2*) in the farmingsuperstructure system (FSS).

FIG. 17H′ shows a cannabinoid extraction system including vessels,filters, pumps, piping connecting flow between vessels and adsorbers,valving, controllers, pressure regulators, metering equipment, flowcontrol, and microprocessor equipment, their construction,implementation, and functionality.

FIG. 17J′ shows one non-limiting embodiment of a cannabinoid emulsionmixing system (17J*).

FIG. 17K′ shows one non-limiting embodiment of a cannabinoid softgelencapsulation system (17K*).

FIG. 18′ shows a simplistic diagram illustrating a multifunctionalcomposition mixing module that is configured to generate amultifunctional composition from at least a portion of Cannabis plants(107*, 207*) that was harvested from each growing assembly (100*, 200*).

FIG. 19′ illustrates a single fully-grown DANLEO III plant.

FIG. 20′ illustrates zoomed-in view of a budding or flowering plant.

FIG. 21′ illustrates a single leaf of DANLEO III.

FIG. 22′ illustrates a trimmed and dried bud (reproductive structure) ofDANLEO III.

FIG. 23′ shows a cannabis cloning assembly (CA*) that is configured toclone cannabis plants and/or DANLEO III (107*, 207*) that were growingin each growing assembly (100*, 200*).

FIG. 1A:

FIG. 1A shows a simplistic block flow diagram of one embodiment of anInsect Production Superstructure System (IPSS) including the sequencesteps of feedstock mixing (step A), feedstock splitting (step B), insectfeeding (step C1, C2), insect breeding (step D), insect collection (stepE), and insect grinding (step F).

FIG. 1A shows a plurality of sequence steps of an Insect ProductionSuperstructure System (IPSS) including, feedstock mixing (step A),feedstock splitting (step B), insect feeding chamber #1 (step C1),insect feeding chamber #2 (step C2), insect breeding (step D), insectcollection (step E), and insect grinding (step F).

Step A involves feedstock mixing where feedstock may be mixed with oneor more additives from the group consisting of water, minerals,vitamins, and polymer to form an enhanced feedstock. Additionally, otherenhancers may be added to the feedstock such as niacin, taurine,glucuronic acid, malic acid, N-acetyl L tyrosine, L-phenylalanine,caffeine, citicoline, or insect growth hormones. Table 1 on FIG. 40lists the types of additives and enhancers that may be mixed with afeedstock to generate an enhanced feedstock.

Generally, a feedstock may be characterized as agriculture residue,alcohol production coproducts, animal waste, bio-waste, compost, cropresidues, energy crops, fermentation waste, meat, insects, fermentativeprocess wastes, food processing residues, food waste, garbage,industrial waste, livestock waste, municipal solid waste, plant matter,poultry wastes, rice straw, sewage, spent grain, spent microorganisms,urban waste, vegetative material, wood waste, cannabis, waste cannabisfrom the Farming Superstructure System, fish, fish that are fed theinsects grown in the IPSS.

Mixing of feedstock with additives or enhancers is discussed below indetail. Exact proportions of feedstock, additives, and enhancers may beprecisely combined to form an enhanced feedstock that is suitable togrow insects in a manner that maximizes productivity, minimizesmortality, and maximizes animal welfare. It has been my realization thatthe enhanced feedstock mixtures, weigh ratios, proportions, ranges citedin Table 1 of FIG. 40 are those that maximize insect production in aminimal amount of space.

It also has been my realization that the enhancers listed herein arethose, when fed to insects, may then subsequently fed to humans asenergy-Insects®, which are a specialized kind of edible insect thatcontains a dose of the stimulant caffeine, vitamins, and otherfunctional ingredients. It has also been my realization that insectstruly enjoy eating my inventive enhanced feedstock blend and itincreases their quality of life. Although there is no evidence and noway of truly telling that insects have the cognitive ability to enjoyeating my proprietary enhanced feedstock blend, I certainly give themthe benefit of the doubt.

It has also been my realization that mixing water with the feedstockprofoundly benefits insects since it elevates their well-being by makingit impossible for them not to fear from expiration from respiratoryimpairment from being drowned in or under a liquid. It is the totalityof the features of the present application that provide the maximumbenefit to society.

An enhanced feedstock transfer line (002) is discharged from feedstockmixing (step A) where it enters the feedstock splitting (step B). Step Bfeedstock splitting involves dividing the enhanced feedstock up into aplurality of enhanced feedstock steams. In embodiments, it may beadvantageous to have a plurality of insect feeding chambers and only onefeedstock mixing sequence step. This minimizes the capital intensity ofthe Insect Production Superstructure System (IPSS) to thus in turnpermits a more lucrative return on investment (ROI). In some instances,Step B may not be required since only one feeding chamber is desired.

A first enhanced feedstock transfer line (004) and a second enhancedfeedstock transfer line (006) are discharged from feedstock splitting(Step B) and are routed to insect feeding chamber #1 (step C1) andinsect feeding chamber #2 (step C2). FIG. 1A discloses a plurality offeeding chamber steps (C1 and C2). Two feeding chambers are shown inFIG. 1A, however it is to be noted that only one may be utilized, orthree (as depicted in FIG. 17), or more may be utilized as seen fit.

Although two feeding chambers are shown in FIG. 1A, it is to be notedthat the egg-laying insects present therein may freely travel from onefeeding chamber to another. This is evidenced by feeding chambertransfer line (008) which connects the insect feeding chamber #1 (stepC1) with insect feeding chamber #2 (step C2). The plurality of feedingchambers and a passageways therebetween encourage egg-laying insectstherein to express normal behavior by enabling mobility and relocationto a more suitable living environment. An insect may decide to up andrelocate for any reason it chooses or no reason at all. In the eventthat one breeding chamber lacks sufficient amounts of enhancedfeedstock, or is over-crowded, or contains diseased or cannibalisticinsects, the insects may relocate to another feeding chamber toalleviate their discomfort, pain, injury, disease, and fear anddistress.

Herein is disclosed an Insect Production Superstructure System (IPSS)that permits insects to have mobility and the opportunity to choosebetween different possible courses of action. Herein are disclosedadvancements and better solutions that meet new requirements,unarticulated needs, or existing market needs in maximizing insectwelfare, maximizing insect output on a minimal physical outlay, andbenefit of large groups of people a high-value animal protein.

FIG. 1A shows a first egg-laden breeding material transfer line (020)and a second egg-laden breeding material transfer line (021) being mixedinto a combined egg-laden breeding material transfer line (022) which isthen in turn provided to insect breeding (step D).

Insect eggs are extracted from the plurality of breeding chambers andare provided to a breeding chamber where the eggs are incubated andhatched. Hatched insects are then provided to the plurality of insectfeeding chambers (step C1 and C2) via a first feeding chamber hatchedinsect transfer line (024) and a second feeding chamber hatched insecttransfer line (026), respectively. Thus, herein is disclosed a methodto: (i) remove at least a portion of eggs laid by the egg-laying insectswithin the feeding chambers; (ii) incubate at least a portion of theremoved eggs in a breeding chamber; (iii) hatch at least a portion ofincubated eggs; and, (iv) introduce a portion of hatched insects backinto the insect feeding chamber.

Generally, the innovative methods of the Insect ProductionSuperstructure System (IPSS) and Farming Superstructure System (FSS) ismore generally suited for insects including one or more selected fromthe group consisting of Anthocoridae, minute pirate bugs, pirate bugs,flower bugs, the genus Orius, omnivorous bugs, carnivorous bugs,Orthoptera order of insects, grasshoppers, crickets, katydids, weta,lubber, acrida, locusts, mites, spider mites, predatory mites,Neoseiulus Fallacis, genus of mites that are in the Phytoseiidae family,arthropods, hexapods, beetles, cicadas, beetles, nematodes, mealworms,cockroaches, bats, mammals of the order Chiroptera, yellow mealwormbeetles, Tenebrio Molitor, Tetranychus Urticae, carnivorous arthropods,omnivorous arthropods, green lacewings, insects in the familyChrysopidae, insects in the order Neuroptera, mantidflies, black soldierflies, butterflies, larvae, fly larvae, insect larvae, arthropod larvae,black soldier fly larvae, Hermetia illucens, antlions, mosquitos,Colorado potato beetle, Leptinotarsa decemlineata, moths, moth larvae,diamondback moth, Plutella xylostella, moth species of the familyPlutellidae and genus Plutella. Encarsia Formosa, Autographacalifornica, alfalfa looper, moths of the family Noctuidae, insects inthe macrolepidopteran clade Rhopalocera from the order Lepidoptera,whitefly parasites, ladybugs, spiders, dragonflies, orb-weaving spiders,arachnids, Spodoptera frugiperda, members of the spider familyAraneidae, praying mantis, arachnids, eight-legged arthropods, andsix-legged arthropods.

Generally, the innovative methods of the Insect ProductionSuperstructure System (IPSS) and Farming Superstructure System (FSS) ismore generally suited for insects including one or more selected fromthe group consisting of lepidoptera, larvae of Lepidoptera, larvae ofbutterflies, silkworm (Bombyx mori), larvae of silkworm (Bombyx mori),cabbage looper moth (Trichoplusia ni), and larvae of cabbage looper moth(Trichoplusia ni).

In embodiments, the bats provide a source of guano which may be used inthe growing medium to grow cannabis plants and/or psilocybin mushrooms.In embodiments, the insects provide a source of guano which may be usedin the growing medium to grow cannabis plants and/or psilocybinmushrooms.

In embodiments, the bats provide a source of guano which may be used inthe growing medium to grow the plants. In embodiments, the bats includebat from families including: Megadermatidae, Craseonycteridae,Rhinopomatidae, Hipposideridae, Rhinolophidae, Miniopteridae,Noctilionidae, Mormoopidae, Mystacinidae, Thyropteridae, Furipteridae,Mormoopidae, Phyllostomidae, Molossidae, Emballonuridae, Myzopodidae,Emballonuridae, Natalidae, Vespertilionidae, and combinations thereof.

In embodiments, the insects feed on insect eggs, insect larva, and otherinsects including living organisms which may or may not contain chitinnot only including spider mites, rust mites, thrips, jumping plant lice,white fly, knats, gnats, aphids, and insects. In embodiments, theinsects feed on thrips order Thysanoptera. In embodiments, the insectsfeed on Tetranychus Urticae. In embodiments, the insects feed on spidermites. In embodiments, the insects eat other insects that are found onthe cannabis plants disclosed herein. In embodiments, the bats eatinsects that are found on the cannabis plants disclosed herein.

Both the insect feeding chamber #1 (step C1) and insect feeding chamber#2 (step C2) are in fluid communication with insect collection (step E).The insect feeding chamber #1 (step C1) is in fluid communication withinsect collection (step E) via a first feeding chamber insect transferline (010). The insect feeding chamber #2 (step C2) is in fluidcommunication with insect collection (step E) via a second feedingchamber insect transfer line (012).

Insects may be collected from the insect feeding chambers in a number ofways. Some non-limiting embodiments of the present disclosure suggestremoving the insects by vibrating the egg-laying insects from thefeeding chamber. Some non-limiting embodiments of the present disclosuresuggest removing the insects by conveying the egg-laying insects fromthe feeding chamber. Some non-limiting embodiments of the presentdisclosure suggest vacuuming the insects from the feeding chamber.

It is to be noted that all of the embodiments disclosed herein arenon-limiting and as long as the insects are in fact removed from aninsect feeding chamber by any conceivable means or method, the bounds ofthis application are deemed to have been infringed. Thus, it should beapparent, however, to those skilled in the art that many moremodifications besides those already described are possible withoutdeparting from the inventive concepts herein related to removing insectsfrom the feeding chamber. The inventive subject matter pertaining toremoving insects from the feeding chambers, therefore, is not to berestricted to vibrating, conveying, vacuuming insects from the feedingchamber but instead extend to any possible means for achieving the endof removing insects from out of the interior of the feeding chamber.

In embodiments, the insect collection (step E) is in fluid communicationwith insect grinding (step F) via a combined collected insect transferline (014). The insect grinding (step F) is configured to output groundinsects via a ground insect transfer line (016).

FIG. 1B:

FIG. 1B elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence steps of pathogen removal (step G) andmultifunctional composition mixing (step H).

FIG. 1B shows a pathogen removal (step G) placed upstream of amultifunctional composition mixing (step H) step. In embodiments, thepathogen removal (step G) is configured to accept collected insectsprovided from the insect collection (step E) or insect grinding (stepF). In embodiments, the pathogen removal (step G) is configured toaccept collected insects provided from the insect collection (step E).In embodiments, the pathogen removal (step G) is configured to acceptcollected insects provided from the insect grinding (step F) as seen inFIG. 13 as accepting ground separated insects (1500). However, it is tobe noted that grinding need not take place in order for pathogen to beremoved from collected insects. As seen in the non-limiting embodimentof FIG. 1B, pathogen removal (step G) only places after insectcollection (step E) and after insect grinding (step F). However, it isnot necessary that grinding takes place in between insect collection(step E) and pathogen removal (step G).

Pathogen removal (step G) is optional. In embodiments, the insects areheated before they are reduced in size by grinding. In embodiments, theinsects are submerged in a water bath before being heated. Inembodiments, the insects are killed before being submerged in a waterbath. In embodiments, the insects are submerged in a water bath andheated simultaneously. In embodiments, the insects are submerged in awater bath of treated water. In embodiments, the insects are submergedin a water bath of treated water, the treated water is treated by atleast two water treatment units. In embodiments, the insects aresubmerged in a water bath of treated water, the treated water is treatedby at least one water treatment units.

Thus, it is the essence of this disclosure to intend that a person ofordinary skill in the art be on notice of my intention to entertain allpossibilities to grinding insects, microwaving them, or suffocating themto death. Nonetheless, grinding can be before pathogen removal. Orpathogen removal can be before grinding. In embodiments, insects may beeuthanized by hypothermia. In embodiments, insects may be euthanized byfreezing them. In embodiments, insects may be euthanized by reducing thetemperature to below 32 degrees Fahrenheit. In embodiments, insects maybe euthanized by reducing the temperature to below 40 degreesFahrenheit. In embodiments, insects may be euthanized by reducing thetemperature to a temperature range selected from the group consistingof: 45 degrees Fahrenheit to 40 degrees Fahrenheit, 40 degreesFahrenheit to 35 degrees Fahrenheit, 35 degrees Fahrenheit to 30 degreesFahrenheit, 30 degrees Fahrenheit to 25 degrees Fahrenheit, 25 degreesFahrenheit to 20 degrees Fahrenheit, 20 degrees Fahrenheit to 15 degreesFahrenheit, 15 degrees Fahrenheit to 10 degrees Fahrenheit, 10 degreesFahrenheit to 5 degrees Fahrenheit, 5 degrees Fahrenheit to 0 degreesFahrenheit, 0 degrees Fahrenheit to −5 degrees Fahrenheit, −5 degreesFahrenheit to −10 degrees Fahrenheit, −10 degrees Fahrenheit to −15degrees Fahrenheit, and less than −15 degrees Fahrenheit.

Pathogen Removal (Step G)

The pathogen removal (step G) involves utilization of a pathogen removalunit to convert a stream of pathogen-laden insects into a stream ofpathogen-depleted insects (1570). The pathogen removal (step G) removespathogens from pathogen-laden insects to form pathogen depleted insectswhich has a reduced amount of pathogens relative to the pathogen-ladeninsects.

In embodiments, insects may be introduced to the interior (6A3) insecttank (6A2) from various locations including: from FIG. 14I and includethe liquid-depleted insects (ISO) that were filtered in the filter(I11); from FIG. 14J and include the liquid-depleted insects (J10, J53)that were discharged from the evaporator (J11); from FIG. 14K andinclude the third separated insects or fourth separated insects (KCX);from FIG. 14K and include the third separated insects or fourthseparated insects (KCX); from FIG. 14K and include the small insectparticulate portion (KCW) or the large insect particulate portion (KCY)that had undergone evaporation by spray drying.

In embodiments, pathogens are comprised of one or more from the groupconsisting of acute respiratory syndrome coronavirus, influenza Aviruses, H5N1, H7N7, avian influenza, foot and mouth disease, bovinespongiform encephalopathy, Q-fever, cutaneous zoonotic leishmaniasis,Ebola, monkeypox, Rift Valley fever, Crimea Congo hemorrhagic fever,encephalopathy, West Nile fever, paramyxoviruses, a virus, bacteria,fungus, prions, and parasites. In embodiments, the virus includes abaculovirus. In embodiments, the baculovirus includes a baculovirusexpression vector (BEV) comprising a recombinant baculovirus that hasbeen genetically modified to lead the expression of a foreign gene. Inembodiment, the foreign gene is that from a human. In embodiments, thebaculovirus includes a polyclonal baculovirus comprising a recombinantbaculovirus. In embodiments, the baculovirus includes an oligoclonalbaculovirus comprising a recombinant baculovirus. In embodiments, thebaculovirus includes a monoclonal baculovirus comprising a recombinantbaculovirus.

In embodiments, the baculovirus includes a genetically modifiedbaculovirus where a gene is inserted into to produce a protein. Thebaculovirus is then introduced to the insects, which are infected andthe virus replicates within the insect. The insect is then grown withinthe IPSS the insects accumulate the desired protein of interest insideof the insect where it is then extracted. In embodiments, the proteinderived from the genetically modified baculovirus is extracted and usedfor a vaccine, antibody, peptide, or chemical. In embodiments, thebaculovirus can be used as a vaccine expression/delivery vector. Inembodiments, the recombinant protein, vaccine, antibody, peptide, orchemical may be used to treat a wide variety of diseases and viruses,such as acute respiratory syndrome coronavirus, coronavirus, coronavirusdisease, influenza A viruses, H5N1, H7N7, avian influenza, foot andmouth disease, bovine spongiform encephalopathy, Q-fever, cutaneouszoonotic leishmaniasis, Ebola, monkeypox, Rift Valley fever, CrimeaCongo hemorrhagic fever, encephalopathy, West Nile fever,paramyxoviruses, a virus, cancer, tetanus, diphtheria, mumps, measles,pertussis (whooping cough), meningitis, and polio. In embodiment, theinsect-derived recombinant protein, vaccine, antibody, peptide, orchemical is a biological preparation that provides active acquiredimmunity to a particular infectious disease.

In embodiments, the virus includes a baculovirus. In embodiments, thebaculovirus includes a baculovirus expression vector (BEV) comprising arecombinant baculovirus that has been genetically modified to lead theexpression of a foreign gene. In embodiment, the foreign gene is thatfrom a cannabis plant, wherein the insect biologically produces acannabinoid, wherein the cannabinoid can be later extracted from theinsect together with insect lipids. In embodiment, the foreign gene isthat from a cannabis plant, wherein the insect biologically produces acannabinoid.

In embodiments, some of the aforesaid pathogens may be present in theinsects that grow within the feeding chamber. It is possible that thewater added to the enhanced feedstock contains pathogens as listed abovewhich the insect's carry-on through to the humans and animals duringconsumption. Thus, it is of paramount importance to mitigate thepossible threats to society that are associated with permittingpathogen-laden water to pass on to humans or animals via thepathogen-laden insects.

In embodiments, pathogens are removed from the insects by theapplication of heat. In embodiments, pathogens are removed by heatinginsects to a temperature range between about 110 degrees Fahrenheit toabout 550 degrees Fahrenheit. In embodiments, pathogens are removed byheating insects to a temperature range between about 120 degreesFahrenheit to about 170 degrees Fahrenheit. In embodiments, pathogensare removed by heating said insects to a temperature range between about171 degrees Fahrenheit to about 250 degrees Fahrenheit. In embodiments,pathogens are removed by heating insects to a temperature range betweenabout 350 degrees Fahrenheit to about 450 degrees Fahrenheit.

In embodiments, pathogens are removed from said insects with microwaveradiation. In embodiments, the microwave radiation is in the form ofvariable frequency microwave radiation. In embodiments, the variablefrequency microwave radiation operates at a frequency between about 2GHz to about 8 GHz. In embodiments, the variable frequency microwaveradiation operates at a frequency of about 2.45 GHz.

In embodiments, the variable frequency microwave radiation operates at apower level between about 30 Watts to about 500 Watts. In embodiments,the variable frequency microwave radiation operates at a power levelbetween about 50 Watts to about 150 Watts. In embodiments, the variablefrequency microwave radiation operates at a power level between about100 Watts to about 200 Watts. In embodiments, pathogens are removed fromsaid insects over a duration of time between about 0.1 seconds to about500 seconds. In embodiments, pathogens are removed from said insectsover a duration of time between about 0.5 seconds to about 15 seconds.In other embodiments, pathogens may be removed by boiling the insects inwater.

FIG. 1A in no way describes every possible embodiment of the pathogenreduction disclosure because describing every possible embodiment wouldbe impractical, if not impossible. FIG. 13 elaborates upon otherpossibilities related to removing pathogens from insects.

Multifunctional Composition Mixing (Step H)

The multifunctional composition mixing (step H) involves mixing theinsects with fiber-starch materials, binding agents, density improvingtextural supplements, moisture improving textural supplements, andoptionally cannabis enhancers, to form a multifunctional composition.The multifunctional composition may be further processed to createfoodstuffs not only including ada, bagels, baked goods, beverages,biscuits, bitterballen, bonda, breads, cakes, candies, cereals, chips,chocolate bars, carbonated soft drinks, carbonated drinks, chocolate,coffee, cokodok, confectionery, cookies, cooking batter, corn starchmixtures, crackers, crêpes, croissants, croquettes, croutons, dolma,dough, doughnuts, energy bars, flapjacks, french fries, frozen custard,frozen desserts, frying cakes, fudge, gelatin mixes, granola bars,gulha, hardtack, ice cream, khandvi, khanom buang, krumpets, meze, mixedflours, muffins, multi-grain snacks, nachos, nian gao, noodles, nougat,onion rings, pakora, pancakes, panforte, pastas, pastries, pie crust,pita chips, pizza, poffertjes, pretzels, protein powders, pudding, ricekrispie treats, sesame sticks, smoothies, snacks, soft drinks, sportdrinks, sparkling drinks, specialty milk, tele-bhaja, tempura, toffee,tortillas, totopo, turkish delights, or waffles.

In embodiments, the fiber-starch materials may be comprised of singularor mixtures of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, or vegetable-based materials. In embodiments, thefiber-starch mass ratio ranges from between about 400 pounds offiber-starch per ton of multifunctional composition to about 1800 poundsof fiber-starch per ton of multifunctional composition.

In embodiments, the binding agents may be comprised of singular ormixtures of agar, agave, alginin, arrowroot, aspartame, carrageenan,collagen, cornstarch, egg whites, finely ground seeds, furcellaran,gelatin, guar gum, honey, katakuri starch, locust bean gum, pectin,potato starch, proteins, psyllium husks, sago, sugars, stevia, syrups,tapioca, vegetable gums, or xanthan gum. In embodiments, the bindingagent mass ratio ranges from between about 33 pounds of binding agentper ton of multifunctional composition to about 600 pounds of bindingagent per ton of multifunctional composition.

In embodiments, the density improving textural supplements may becomprised of singular or mixtures of extracted arrowroot starch,extracted corn starch, extracted lentil starch, extracted potato starch,or extracted tapioca starch. In embodiments, the density improvingtextural supplement mass ratio ranges from between about 5 pounds ofdensity improving textural supplement per ton of multifunctionalcomposition to about 300 pounds of density improving textural supplementper ton of multifunctional composition.

In embodiments, the moisture improving textural supplements may becomprised of singular or mixtures of almonds, brazil nuts, cacao,cashews, chestnuts, coconut, filberts, hazelnuts, Indian nuts, macadamianuts, nut butters, nut oils, nut powders, peanuts, pecans, pili nuts,pine nuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tigernuts, walnuts, and vanilla. In embodiments, the moisture improvingtextural supplement mass ratio ranges from between about 5 pounds ofmoisture improving textural supplement per ton of multifunctionalcomposition to about 300 pounds of moisture improving texturalsupplement per ton of multifunctional composition.

In embodiments, a cannabis enhancer may be added to the multifunctionalcomposition. The cannabis enhancer may be marijuana in a powdered,dried, ground, or decarboxylated form. In embodiments, the cannabisenhancer may be remnants of vaporization, such as substantially fixedcarbon feedstock components. In embodiments, the cannabis enhancer maybe comprised of volatile feedstock components and a solvent. Inembodiments, the cannabis enhancer may be comprised of volatilefeedstock components and an alcohol. The cannabis enhancer may becomprised of volatile feedstock components and fixed carbon feedstockcomponents. In embodiments, cannabis enhancer may be comprised ofvolatile feedstock components. In embodiments, cannabis enhancer may becomprised of fixed carbon feedstock components. In embodiments, thecannabis enhancer contains tetrahydrocannabinol (THC) in a mixture ofvolatile feedstock components and fixed carbon feedstock components.

In embodiments, the multifunctional composition ranges from betweenabout 1800 pounds of cannabis enhancer per ton of multifunctionalcomposition to about 1995 pounds of cannabis enhancer per ton ofmultifunctional composition. In embodiments, the volatile feedstockcomponent mass ratio ranges from between about 500 pounds of volatilefeedstock components per ton of cannabis enhancer to about 2000 poundsof volatile feedstock components per ton of cannabis enhancer. Inembodiments, the volatile feedstock component mass ratio ranges frombetween about 500 pounds of volatile feedstock components per ton ofmultifunctional composition to about 1750 pounds of volatile feedstockcomponents per ton of multifunctional composition. In embodiments, thefixed carbon feedstock component mass ratio ranges from between about100 pounds of fixed carbon feedstock components per ton of cannabisenhancer to about 1700 pounds of fixed carbon feedstock components perton of cannabis enhancer. In embodiments, the fixed carbon feedstockcomponent mass ratio ranges from between about 100 pounds of fixedcarbon feedstock components per ton of multifunctional composition toabout 1600 pounds of fixed carbon feedstock components per ton ofmultifunctional composition.

Accordingly, I wish to make my intentions clear—and at the same time putpotential competitors on clear public notice. It is my intent that thisportion of the specification especially relating to multifunctionalcomposition mixing and all claims pertaining thereto receive a liberalconstruction and be interpreted to uphold and not destroy my rights asinventor. It is my intent that the claim terms be construed in acharitable and common-sensical manner, in a manner that encompasses theembodiments disclosed in this and other portions of the specificationand drawings relating to multifunctional composition mixing withoutincorporating unrecited, unnecessary limitations. It is my intent thatthe specification relating to multifunctional composition mixing claimterms be construed as broadly as practicable while preserving thevalidity of the claims. It is my intent that the claim terms beconstrued in a manner consistent with the context of the overall claimlanguage and this portion of the specification along with FIGS. 1B and12A, without importing extraneous limitations from the specification orother sources into the claims, and without confining the scope of theclaims to the exact representations depicted in the specification ordrawings in FIGS. 1B and 12A. It is also my intent that not each andevery term of the claim be systematically defined and rewritten. Claimterms and phrases should be construed only to the extent that it willprovide helpful, clarifying guidance to the jury, or to the extentneeded to resolve a legitimate, good faith dispute that is material tothe questions of validity or infringement. Otherwise, simple claim termsand phrases should be presented to the jury without any potentiallyconfusing and difficult-to-apply definitional construction.

FIG. 1C:

FIG. 1C elaborates upon the non-limiting embodiment of FIG. 1 furtherincluding the sequence step of lipid extraction (step J).

FIG. 1C shows lipid extraction (step J) downstream of the each of thesteps insect collection (step E), insect grinding (step F), and pathogenremoval (step G).

The lipid extraction (step J) is configured to produce extracted lipids(028) from insects that were previously fed an enhanced feedstock. Inembodiments, the insect fat mass ratio ranges from between about 100pounds of fat per ton of insects produced to about 1800 pounds of fatper ton of insects produced. The egg-laying insects that are presentwithin each feeding chambers, and those that are collected, optionallyground, and optionally exposed to a pathogen removal step areintentionally engineered by feeding an enhanced feedstock to possess awide-ranging fat content ranging from between about 5% to about 90% byweight of insects produced.

In embodiments, the feeding chamber produces insects having fatty acidsincluding palmitic acid, linoleic acid, alpha-linoleic acid, oleic acid,gamma-linoleic acid, or stearic acid. The fatty acids of the insectsthat are fed the enhanced feedstock are lipids. The extraction and useof lipids has many beneficial applications in society involvingmedicine, nanotechnology, consumer products, and chemical productionwith minimal water, feedstock, and environmental impact.

Palmitoleic acid produced from palmitic acid is used to increase insulinsensitivity by suppressing inflammation, reduce inflammation associatedwith eczema. It is also used in cosmetic products, medical products, andcan preserve and treat leather. Linoleic acid is used in oil paints andvarnishes and is used in quick-drying oils. It can be used to reduceacne. It has moisture retentive properties and is used to make lotionsand soaps (silky feel). It is an essential fatty acid and an emulsifier.Alpha-Linolenic acid is an essential dietary requirement linked tocardiovascular health. Oleic acid is used in hair dyes and soaps(slippery feel). It is also used as a food additive. It is used tomanufacture surfactants, soaps, and plasticizers. It is an emulsifyingagent in foods and pharmaceuticals. It can penetrate the skin. It canact as an herbicide, insecticide, and fungicide. It can be used in ametallic soap and with copper to clean mildew. Gamma-Linolenic acid canhelp prevent nerve damage. Stearic acid is used in foundation, babylotions, oils, powders, creams, shaving cream, body and hand cream,cleansers, foot powders, sprays, moisturizers, and soaps (hardness).Stearic acid is a thickener used to make creams, oil pastels, hardcandies, and candles. It is a surfactant. It can be used as a lubricantadditive in plasticized PVC compounds to aid processing. It is also usedto make metallic soaps.

Rubber grade stearic acid can be used as a mold release lubricant forsintering, pressing ceramic powders, and latex foam. It is also used asa thickener in greases. It can be used as a viscosity modifier for oilextraction. Stearic acid combined with castor oil is used to makesofteners for textile sizing. It can be used as a yarn lubricant.Isopropyl Palmitate is in baby lotion/powder/cream, foot powders andsprays. Glyceryl stearate is in nail products, tonics and dressings,cologne/perfumes, concealers, baby lotion/powder/cream, aftershave.Sorbitan stearate is in blush. TEA-Stearate is in mascara. Stearylalcohol is in hair conditioner, hair straighteners and relaxers, tonicsand dressings (help to style hair). Oleyl alcohol is in hairstraighteners and relaxers, and concealers.

Lipids extracted from insects may also be used in emerging areas ofnanotechnology having uses in many areas covering chemistry,engineering, materials science, physics and biology. In coming years,science will continue to develop and increasingly appreciate sources offatty acids derived from insects. For example, investigators are nowseriously focusing on insect derived fatty acids for use in biomedicalsciences, such as bio-imaging, sensing and diagnosis of pathologies atearly stages, targeted drug delivery, and for use with nano-devices thatinteract with the plasma eukaryotic or even prokaryotic cell membranes.

Herein are disclosed systems and methods for obtaining, in massquantities, commercial scale output of insect based lipids for use in avariety of areas throughout society. In embodiments, the lipidextraction (step J) utilizes a lipid extraction unit to extract lipidsfrom insects.

In embodiments, the lipid extraction unit is configured to extractlipids by use of a first immiscible liquid and a second immiscibleliquid. In embodiments, the first immiscible liquid has a first densityand a first molecular weight, and the second immiscible liquid has asecond density and a second molecular weight. In embodiments, firstdensity is greater than the second density. In embodiments, firstmolecular weight is greater than the second molecular weight. Inembodiments, a first immiscible liquid and lipid mixture is formed whichis comprised of a lipid portion and a first immiscible liquid portion.In embodiments, second immiscible liquid and particulate mixture isformed which is comprised of a particulate portion and a secondimmiscible liquid portion. In embodiments, the particulate portion iscomprised of one or more from the group consisting of insect legs, andwings, and protein.

FIG. 1D:

FIG. 1D includes one non-limiting embodiment of an insect traceabilitysystem flow chart. In embodiments, the present disclosure provides foran insect traceability system. In embodiments, the insect traceabilitysystem is specifically tailored towards the unique challenges related totracking, accountability, food safety, and state and federal governmentcompliance of the insect industry, either for food (for humans oranimals), drugs, chemicals, and medicine. In embodiments, the presentdisclosure provides for an insect traceability system that is used toverify the history, location, or application of an item by means ofdocumented recorded identification. In embodiments, the insecttraceability system flow chart may also be a traceability system totrace the cloning, growing, processing of cannabis plants.

In embodiments, the insect traceability system has been developed totrack inventory to end-product (whole insects, ground insects, liveinsects, of insect-related end-products including but not limited tofermented insects, biopolymers, lipids, chemicals, foodstuffs,hydrogenated lipids, etc.). In embodiments, the insect traceabilitysystem includes an insect end-product laboratory analytical testingcomponent.

In embodiments, the present disclosure provides for a cannabis, insect,of foodstuff or beverage traceability system. In embodiments, thetraceability system includes a server having tables comprising adatabase for receiving, processing and storing data. In embodiments, thetraceability system includes a computer network providing electroniccommunication between the server and other computers and/or mobiledevices.

In embodiments, the traceability system tracks data including: (A) timesand dates insects are born fed, watered, bred, killed, suffocated,frozen, sold, leased, borrowed, processed, heated, ground, spray dried,oxidized, hydrolyzed, filtered, evaporated, pressurized, fermented,mixed with water, liquid, gas, acid, enzyme, fungus, cannabis, THC, afiber-starch material, a binding agent, a density improving texturalsupplement, a moisture improving textural supplement, and other insects(either whole, ground, powder, slurry, particulate, frozen, heated,dehydrated, cooked, raw, ground, whole); (B) breeding material moisture,feeding/breeding chamber temperature, humidity, mass/length/width ofeach insect, average insect mass/length/width, genus, species; (C)entity purchased (product, insect, plant, seeds, eggs, clone, foodstuff,beverage, ingredients, compositions), end customer; insect breedingcycle time, temp, humidity, breeding material, moisture and temperatureof breeding material., bacteria content of breeding material, pH);insect feedstock ingredients (composition, vendor information, MSDS).

FIG. 1D includes one non-limiting embodiment of an insect traceabilitysystem flow chart. First, the initial inventory is tracked, including:insect eggs, insects, insects at various stages of development, breedingmaterial, water, water treatment unit (adsorbent, catalyst, ion-exchangeresin, polymer, alumina, etc.), odor control system (adsorbent, sorbent,filter element), enzymes, solvents, chemicals, acid, biocatalysts.

Second, the insects are grown within the insect production system. Thegrown insects may be live, whole, frozen, dried, ground,pathogen-depleted, heated to form a first end-product. Various wastesare generated while making the first end-product. In embodiments, thewastes include insect frass, insect feedstock, insect enhancedfeedstock, spent breeding material (that can no longer be re-used),nonregenerable adsorbent, catalyst, ion-exchange resin, polymer,alumina, or filters. In embodiments, some of the waste is discarded. Inembodiments, some of the waste is sold or recycled. In embodiments, theinsect frass includes solid excreta of insects. In embodiments, theinsect frass includes feedstock materials. In embodiments, the insectfrass includes enhanced feedstock materials. In embodiments, the insectfrass includes water. In embodiments, the insect frass may be used as afertilizer. In embodiments, the insect frass may be used as a fertilizerfor the cannabis plants disclosed in Volume II below.

In embodiments, the insect frass may be used as a fertilizer and appliedat a ratio ranging from 0.10 pounds of frass per 100 square feet, to0.15 pounds of frass per 100 square feet, to 0.25 pounds of frass per100 square feet, to 0.35 pounds of frass per 100 square feet, to 0.45pounds of frass per 100 square feet, to 0.55 pounds of frass per 100square feet, to 0.65 pounds of frass per 100 square feet, to 0.75 poundsof frass per 100 square feet, to 0.85 pounds of frass per 100 squarefeet, to 0.95 pounds of frass per 100 square feet, to 1 pounds of frassper 100 square feet, to 1.15 pounds of frass per 100 square feet, to1.25 pounds of frass per 100 square feet, to 1.35 pounds of frass per100 square feet, to 1.45 pounds of frass per 100 square feet, to 1.55pounds of frass per 100 square feet, to 1.65 pounds of frass per 100square feet, to 1.75 pounds of frass per 100 square feet, to 1.85 poundsof frass per 100 square feet, to 1.95 pounds of frass per 100 squarefeet, to 3 pounds of frass per 100 square feet, to 3 pounds of frass per100 square feet, to 3.15 pounds of frass per 100 square feet, to 3.25pounds of frass per 100 square feet, to 3.35 pounds of frass per 100square feet, to 3.45 pounds of frass per 100 square feet, to 3.55 poundsof frass per 100 square feet, to 3.65 pounds of frass per 100 squarefeet, to 3.75 pounds of frass per 100 square feet, to 3.85 pounds offrass per 100 square feet, to 3.95 pounds of frass per 100 square feet,to 4 pounds of frass per 100 square feet, to 4 pounds of frass per 100square feet, to 4.15 pounds of frass per 100 square feet, to 4.25 poundsof frass per 100 square feet, to 4.35 pounds of frass per 100 squarefeet, to 4.45 pounds of frass per 100 square feet, to 4.55 pounds offrass per 100 square feet, to 4.65 pounds of frass per 100 square feet,to 4.75 pounds of frass per 100 square feet, to 4.85 pounds of frass per100 square feet, to 4.95 pounds of frass per 100 square feet, to 5pounds of frass per 100 square feet. In embodiments, the insect frassmay be used as a fertilizer to fertilize cannabis plants and/orpsilocybin mushrooms.

In embodiments, the insect frass includes: a nitrogen content rangingfrom 1.0 weight percent to 1.5 weight percent, 1.5 weight percent to 2.0weight percent, 2.0 weight percent to 2.5 weight percent, 2.5 weightpercent to 3.0 weight percent, 3.0 weight percent to 3.5 weight percent,3.5 weight percent to 4.0 weight percent, 4.0 weight percent to 4.5weight percent, or 4.5 weight percent to 5.0 weight percent; aphosphorus content ranging from 1.0 weight percent to 1.5 weightpercent, 1.5 weight percent to 2.0 weight percent, 2.0 weight percent to2.5 weight percent, 2.5 weight percent to 3.0 weight percent, 3.0 weightpercent to 3.5 weight percent, 3.5 weight percent to 4.0 weight percent,4.0 weight percent to 4.5 weight percent, or 4.5 weight percent to 5.0weight percent; a potassium content ranging from 1.0 weight percent to1.5 weight percent, 1.5 weight percent to 2.0 weight percent, 2.0 weightpercent to 2.5 weight percent, 2.5 weight percent to 3.0 weight percent,3.0 weight percent to 3.5 weight percent, 3.5 weight percent to 4.0weight percent, 4.0 weight percent to 4.5 weight percent, or 4.5 weightpercent to 5.0 weight percent; and a total nitrogen-phosphorus-potassiumcontent ranging from 1.0 weight percent to 1.5 weight percent, 1.5weight percent to 2.0 weight percent, 2.0 weight percent to 2.5 weightpercent, 2.5 weight percent to 3.0 weight percent, 3.0 weight percent to3.5 weight percent, 3.5 weight percent to 4.0 weight percent, 4.0 weightpercent to 4.5 weight percent, 4.5 weight percent to 5.0 weight percent,5.0 weight percent to 5.5 weight percent, 5.5 weight percent to 6.0weight percent, 6.0 weight percent to 6.5 weight percent, 6.5 weightpercent to 7.0 weight percent, 7.0 weight percent to 7.5 weight percent,7.5 weight percent to 8.0 weight percent, 8.0 weight percent to 8.5weight percent, 8.5 weight percent to 9.0 weight percent, 9.0 weightpercent to 9.5 weight percent, 9.5 weight percent to 10.0 weightpercent, 10.0 weight percent to 10.5 weight percent, 10.5 weight percentto 11.0 weight percent, 11.0 weight percent to 11.5 weight percent, 11.5weight percent to 12.0 weight percent, 12.0 weight percent to 12.5weight percent, 12.5 weight percent to 13.0 weight percent, 13.0 weightpercent to 13.5 weight percent, 13.5 weight percent to 14.0 weightpercent, 14.0 weight percent to 14.5 weight percent, or 14.5 weightpercent to 15.0 weight percent.

Quality testing takes place to ensure that recalls may be instituted ifnecessary. In embodiments, the quality testing includes testing theend-product prior to entering the stream of interstate commerce for: pH,chemicals, contaminants, bacteria, pathogens, yeast, mold, or allergens.

In embodiments, the insect traceability system includes a qualityanalysis of an that includes: a nitrate (NO3) concentration having amaximum level of 1,000 mg NO3/kg of end-product; a mycotoxin analysisincluding: an ochratoxin A concentration having a maximum level of 10μg/kg of end-product; a deoxynivalenol concentration having a maximumlevel of 2,000 μg/kg of end-product; a zearalenone concentration havinga maximum level of 275 μg/kg of end-product; a fumonisins concentrationhaving a maximum level of 2,500 μg/kg of end-product; a metals analysisincluding: a lead concentration having a maximum level of 0.5 mg/kg ofend-product; a cadmium concentration having a maximum level of 0.5 mg/kgof end-product; a mercury concentration having a maximum level of 0.5mg/kg of end-product; a 3-monochloropropane-1,2-diol (3-MCPD)concentration having a maximum level of 20 μg/kg of end-product; adioxins and polychlorinated biphenyls (PCBs) concentration having amaximum level of 3 picogram/gram; a polycyclic aromatic hydrocarbonconcentration having a maximum level of 5 μg/kg of end-product; abenzo(a)pyrene concentration having a maximum level of 2 or 5 μg/kg ofend-product; a total concentration of benzo(a)pyrene, benz(a)anthracene,benzo(b)fluoranthene and chrysene having a maximum level of 15 or 30μg/kg of end-product.

In embodiments, the insect traceability system includes a qualityanalysis of an that includes: a standard plate count (to test for totalaerobic bacterial and total mold and yeasts) having less than: 500,000colony forming unit per gram, 400,000 colony forming units per gram,300,000 colony forming units per gram, 200,000 colony forming units pergram, 100,000 colony forming units per gram, 50,000 colony forming unitsper gram, 25,000 colony forming units per gram, or 5,000 colony formingunits per gram; a coliform content less than 500 colony forming unitsper gram, 400 colony forming units per gram, 300 colony forming unitsper gram, 200 colony forming units per gram, 100 colony forming unitsper gram, 90 colony forming units per gram, 80 colony forming units pergram, 70 colony forming units per gram, 60 colony forming units pergram, 50 colony forming units per gram, 40 colony forming units pergram, 30 colony forming units per gram, 20 colony forming units pergram, or 10 colony forming units per gram; a coliform content less than500,000 colony forming unit per gram, 400,000 colony forming units pergram, 300,000 colony forming units per gram, 200,000 colony formingunits per gram, 100,000 colony forming units per gram, 50,000 colonyforming units per gram, 25,000 colony forming units per gram, or 5,000colony forming units per gram; a spore-forming sulphite reducinganaerobe content less than 500 colony forming units per gram, 400 colonyforming units per gram, 300 colony forming units per gram, 200 colonyforming units per gram, 100 colony forming units per gram, 90 colonyforming units per gram, 80 colony forming units per gram, 70 colonyforming units per gram, 60 colony forming units per gram, 50 colonyforming units per gram, 40 colony forming units per gram, 30 colonyforming units per gram, 20 colony forming units per gram, or 10 colonyforming units per gram; a spore-forming sulphite reducing anaerobecontent less than 500,000 colony forming unit per gram, 400,000 colonyforming units per gram, 300,000 colony forming units per gram, 200,000colony forming units per gram, 100,000 colony forming units per gram,50,000 colony forming units per gram, 25,000 colony forming units pergram, or 5,000 colony forming units per gram; a Pseudomonas aeruginosacontent less than 500 colony forming units per gram, 400 colony formingunits per gram, 300 colony forming units per gram, 200 colony formingunits per gram, 100 colony forming units per gram, 90 colony formingunits per gram, 80 colony forming units per gram, 70 colony formingunits per gram, 60 colony forming units per gram, 50 colony formingunits per gram, 40 colony forming units per gram, 30 colony formingunits per gram, 20 colony forming units per gram, or 10 colony formingunits per gram; a Pseudomonas aeruginosa content less than 500,000colony forming unit per gram, 400,000 colony forming units per gram,300,000 colony forming units per gram, 200,000 colony forming units pergram, 100,000 colony forming units per gram, 50,000 colony forming unitsper gram, 25,000 colony forming units per gram, or 5,000 colony formingunits per gram; a E. coli content less than 500 colony forming units pergram, 400 colony forming units per gram, 300 colony forming units pergram, 200 colony forming units per gram, 100 colony forming units pergram, 90 colony forming units per gram, 80 colony forming units pergram, 70 colony forming units per gram, 60 colony forming units pergram, 50 colony forming units per gram, 40 colony forming units pergram, 30 colony forming units per gram, 20 colony forming units pergram, or 10 colony forming units per gram; a E. coli content less than500,000 colony forming unit per gram, 400,000 colony forming units pergram, 300,000 colony forming units per gram, 200,000 colony formingunits per gram, 100,000 colony forming units per gram, 50,000 colonyforming units per gram, 25,000 colony forming units per gram, or 5,000colony forming units per gram.

Fourth, after the initial inventory has passed product testing they maybe further processed to make a second end-product from the first-endproduct. In embodiments, the second end-product includes insects thatare tested for quality in the form of live, whole, frozen, dried,ground, pathogen-depleted, or heated insects. In embodiments, the secondend-product includes a multifunctional composition, a foodstuff, lipids,lipid intermediate products, lipid consumer products, beverages,alcoholic beverages, emulsions, or consumer products. In embodiments,the second end-product includes a first end-product. In embodiments, thesecond end-product includes anything but a first end-product.

Fifth, a detailed transportation manifest is created prior to shipmentthe second end-product into the stream of commerce. In embodiments, thetransportation manifest includes: origin of shipment, destination ofshipment, detailed list of shipment contents shipper address, receiveraddress, date shipped, date received, and displaying the entire chain ofcustody. Sixth, the transporter name and license number is entered intothe insect traceability system. Seventh, the retailer name and addressis entered into the insect traceability system. Eighth, the consumername and address is entered into the insect traceability system.

In embodiments, the insect traceability system provides a log to trackinsects and/or each batch of insects or each end-product. Inembodiments, the insect traceability system logs insects grown in theInsect Production Superstructure System (IPSS) by used of a barcode orradio-frequency identification (RFID). In embodiments, the RFID useselectromagnetic fields to automatically identify and track tags attachedto batches of insects. Each insect feeding chamber includes a tag thatcontains electronically-stored information such as: time and date theinsects were hatched, time and date the insects were harvested, insectfeed composition and ingredients, growing medium moisture, feedingchamber temperature and humidity, mass of each insect, mass increaseover time of each feeding chamber, species/genus of each insect,end-customer, quality assurance records, insect water quality. Inembodiments, the insect traceability system provides for an audit trailfor state and federal laws, rules, and regulations and makes recallspossible.

FIG. 2:

FIG. 2 shows a non-limiting embodiment of an enhanced feedstock mixingmodule (1000) including a feedstock distribution module (1A), mineraldistribution module (1B), vitamin distribution module (1C), polymerdistribution module (1D), water distribution module (1E), and anenhanced feedstock distribution module (1F).

FIG. 2 displays a computer (COMP) that is integral to the InsectProduction Superstructure System (IPSS). The computer (COMP) isconfigured to accept a variety of signals from process variables using avariety of sensors and/or controllers, and then apply advanced processlogic control methodologies, strategies and/or sequences to realizemodulation of actuators and/or valves to effectuate optimal operation ofthe Insect Production Superstructure Systems (IPSS) and its associatedmodules not only including feedstock mixing, feedstock splitting, insectfeeding, insect breeding, insect collection, insect grinding, pathogenremoval, multifunctional composition mixing, and lipid extractionmodules. A variety of signals are sent to and from the computer (COMP)to a variety of controllers, sensors, valves, motors, actuators, and thelike distributed throughout the entire Insect Production SuperstructureSystem (IPSS).

The computer (COMP) applies the control approach and methodology for theeach and every entire control loop on a continuous basis, a discretebasis, or a hybrid combination of a continuous basis and a discretebasis. Further, a computer may be applied to implement the controlmethodology by utilizing process variables obtained by either acontinuous sensor, a discrete sensor, or a combination of a continuoussensor and a discrete sensor and hold the control action at a constantset-point at that specific control output until a later time when thatcontrol algorithm is executed. The time between successiveinterrogations or application of the control algorithm is applied by thecontrol computer is defined as the control interval. The controlinterval for a continuous sensor is typically shorter than that of adiscrete sensor and based upon commercially available mechanical,electrical, or digital continuous or discrete sensors, the controlinterval or control time can vary from 0.2 milliseconds, to 0.5 seconds,to 1.0 second, to 10 seconds, to 30 seconds, to 1 minute, to 5 minutes,to 10 minutes, to 30 minutes, to 1 hour, to 10 hours, or longer. Theoutput from the control computer is transmitted to a controller device.From application of the control logic, the control computer can send avariety of signals to a variety of controllers.

In embodiments, the signals from controllers or sensors are inputted oroutputted to and from a computer (COMP) by a user or operator via aninput/output interface (I/O) as disclosed in FIG. 2 and many others (notonly including FIGS. 3, 5, 6, 7, 8, 9, 10, 11, 12A, 12B, 13, 14A, 14B,14C, 14D, 14E, 14F, 14G, 14H, 14I, 14J, 15, 16, 17, 18, 19, 20, 21, 22,23, 24, 25, 26, 27A, 27B, 28A, 28B, 29-48). Program and sequencinginstructions may be executed to perform particular computationalfunctions such as automated operation of the valves, actuators,controllers, motors, or the like. In one exemplary embodiment, acomputer (COMP) includes a processor (PROC) coupled to a system memory(MEM) via an input/output interface (I/O). The processor (PROC) may beany suitable processor capable of executing instructions. System memory(MEM) may be configured to store instructions and data accessible byprocessor (PROC). In various embodiments, system memory (MEM) may beimplemented using any suitable memory technology. In all illustratedembodiments, program instructions and data implementing desiredfunctions are shown stored within system memory (MEM) as code (CODE). Inembodiments, the I/O interface (I/O) may be configured to coordinate I/Otraffic between processor (PROC) and system memory (MEM). In someembodiments, the I/O interface (I/O) is configured for a user oroperator to input necessary sequencing protocol into the computer (COMP)for process execution, including sequence timing and repetition of agiven number of states to realize a desired sequence of steps and/orstates. In embodiments, the signals operatively coupled to a controller,valve, actuator, motor, or the like, may be an input value to be enteredinto the computer (COMP) by the I/O interface (I/O). In embodiments, thecomputer (COMP) includes a small single-board computer such as aRaspberry Pi developed in the United Kingdom by the Raspberry PiFoundation. The system is fully flexible to be tuned, configured, andoptimized to provide an environment for scheduling the appropriateprocess parameters by programmatically controlling the opening andclosing of valves at specific time intervals, or strategically andsystematically opening, closing, turning on, turning off, modulating,controlling, or operating motors, valves, or actuators at specific timeintervals at specific times. In embodiments, a user or operator maydefine control loops, cycle times, step numbers, and states which may beprogrammed into the computer (COMP) by an operator accessibleinput/output interface (I/O).

Feedstock Distribution Module (1A)

FIG. 2 displays a feedstock distribution module (1A) including afeedstock tank (1A2) that is configured to accept a feedstock (1A1). Thefeedstock tank (1A2) has an interior (1A3), a feedstock input (1A4), afeedstock conveyor (1A5), and a feedstock conveyor output (1A6). Thefeedstock tank (1A2) accepts a feedstock (1A1) to the interior (1A3) andregulates and controls an engineered amount of feedstock (1A1)downstream to be mixed to form an enhanced feedstock. The feedstockconveyor (1A5) has an integrated feedstock mass sensor (1A7) that isconfigured to input and output a signal (1A8) to the computer (COMP).The feedstock conveyor motor (1A9) has a controller (1A10) that isconfigured to input and output a signal (1A11) to the computer (COMP).The feedstock mass sensor (1A7), feedstock conveyor (1A5), and feedstockconveyor motor (1A9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of feedstock (1A1) via afeedstock transfer line (1A14). A feedstock moisture sensor (1A12A) ispreferably installed on the feedstock transfer line (1A14) and isconfigured to input a signal (1A13A) to the computer (COMP).

In embodiments, the insect feeding chamber may operate at an enhancedfeedstock to insect ratio ranging from between about 1 ton of enhancedfeedstock per ton of insects produced to about 5 tons of enhancedfeedstock per ton of insects produced. In embodiments, about 1 ton ofenhanced feedstock can yield about 1 ton of insects. In embodiments,about 2 tons of enhanced feedstock can yield about 1 ton of insects. Inembodiments, about 3 tons of enhanced feedstock can yield about 1 ton ofinsects. In embodiments, about 4 tons of enhanced feedstock can yieldabout 1 ton of insects. In embodiments, about 5 tons of enhancedfeedstock can yield about 1 ton of insects.

Mineral Distribution Module (1B)

FIG. 2 displays a mineral distribution module (1B) including a mineraltank (1B2) that is configured to accept minerals (1B1). The mineral tank(1B2) has an interior (1B3), a mineral input (1B4), a mineral conveyor(1B5), and a mineral conveyor output (1B6). The mineral tank (1B2)accepts minerals (1B1) to the interior (1B3) and regulates and controlsan engineered amount of minerals (1B1) downstream to be mixed to form anenhanced feedstock. The mineral conveyor (1B5) has an integrated mineralmass sensor (1B7) that is configured to input and output a signal (1B8)to the computer (COMP). The mineral conveyor motor (1B9) has acontroller (1B10) that is configured to input and output a signal (1B11)to the computer (COMP). The mineral mass sensor (1B7), mineral conveyor(1B5), and mineral conveyor motor (1B9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of minerals (1B1)via a mineral transfer line (1B12).

Vitamin Distribution Module (1C)

FIG. 2 displays a vitamin distribution module (1C) including a vitamintank (1C2) that is configured to accept vitamins (1C1). The vitamin tank(1C2) has an interior (1C3), a vitamin input (1C4), a vitamin conveyor(105), and a vitamin conveyor output (106). The vitamin tank (1C2)accepts vitamins (1C1) to the interior (1C3) and regulates and controlsan engineered amount of vitamins (1C1) downstream to be mixed to form anenhanced feedstock. The vitamin conveyor (105) has an integrated vitaminmass sensor (1C7) that is configured to input and output a signal (1C8)to the computer (COMP). The vitamin conveyor motor (1C9) has acontroller (1C10) that is configured to input and output a signal (1C11)to the computer (COMP). The vitamin mass sensor (1C7), vitamin conveyor(105), and vitamin conveyor motor (1C9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of vitamins (1C1)via a vitamin transfer line (1C12).

Polymer Distribution Module (1D)

FIG. 2 displays a polymer distribution module (1D) including a polymertank (1D2) that is configured to accept polymer (1D1). The polymer tank(1D2) has an interior (1D3), a polymer input (1D4), a polymer conveyor(1D5), and a polymer conveyor output (1D6). The polymer tank (1D2)accepts polymer (1D1) to the interior (1D3) and regulates and controlsan engineered amount of polymer (1D1) downstream to be mixed to form anenhanced feedstock. The polymer conveyor (1D5) has an integrated polymermass sensor (1D7) that is configured to input and output a signal (1D8)to the computer (COMP). The polymer conveyor motor (1D9) has acontroller (1D10) that is configured to input and output a signal (1D11)to the computer (COMP). The polymer mass sensor (1D7), polymer conveyor(1D5), and polymer conveyor motor (1D9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of polymer (1D1)via a polymer transfer line (1D12). For the context of this disclosure apolymer (1D1) includes exoskeletons of insects separated from anyplurality of separators (S1, S2, S3) contained within the insectevacuation module (3000). For the context of this disclosure a polymer(1D1) includes chitin having the formula of (C8H13O5N)n which is along-chain polymer of an N-acetylglucosamine, a derivative of glucose,and is found in many places throughout the natural world. Chitin is apolymer and a characteristic component of the cell walls of fungi, theexoskeletons of arthropods such as crustaceans (e.g., crabs, lobstersand shrimps) and insects, the radulae of mollusks, and the beaks andinternal shells of cephalopods, including squid and octopuses and on thescales and other soft tissues of fish and lissamphibians. Where recycleof the exoskeletons from the insect evacuation module (3000) to theinsect feeding module (2000) is not possible the polymer (1D1) includesfish scales, fungi, cephalopod shells, cephalopod beaks, Lissamphibiashells, or keratin. In its pure, unmodified form, chitin is translucent,pliable, resilient, and quite tough.

Water Distribution Module (1E)

FIG. 2 illustrates one non-limiting embodiment of a water distributionmodule (1E) that removes contaminants from water (1E1) prior to mixingto form an enhanced feedstock. A source of water (1E1) is routed througha water input line (1E4) and through a first water treatment unit (1E6)and a second water treatment unit (1E11) and into the interior (1E17) ofa water tank (1E16) where it is then pumped via a water supply pump(1E22), though a water control valve (1E36) and then mixed withfeedstock (1A1), minerals (1B1), vitamins (1C1), and polymer (1D1) toform an enhanced feedstock. In embodiments, enhancers (1E44) may beadded to the interior (1E17) of the water tank (1E16). In embodiments,the enhancers (1E44) may include niacin, taurine, glucuronic acid, malicacid, N-acetyl L tyrosine, L-phenylalanine, caffeine, citicoline, insectgrowth hormones, or steroids, or human growth hormones.

A first water pressure sensor (1E2) is positioned on the water inputline (1E4) and is configured to input a signal (1E3) to the computer(COMP). In embodiments, contaminant-laden water (1E5) is routed throughthe water input line (1E4) and transferred to the first water treatmentunit (1E6) via a first water treatment unit input (1E7). The first watertreatment unit (1E6) has a first water treatment unit input (1E7) and afirst water treatment unit output (1E8) and is configured to removecontaminants from the contaminant-laden water (1E5) to form a stream offirst contaminant-depleted water (1E9) that is outputted via a firstcontaminant-depleted water transfer line (1E10). In embodiments, a firstcontaminant-depleted water (1E9) is routed through the firstcontaminant-depleted water transfer line (1E10) and transferred to thesecond water treatment unit (1E11) via a second water treatment unitinput (1E12). The second water treatment unit (1E11) has a second watertreatment unit input (1E12) and a second water treatment unit output(1E13) and is configured to remove contaminants from the firstcontaminant-depleted water (1E9) to form a stream of secondcontaminant-depleted water (1E14) that is outputted via a secondcontaminant-depleted water transfer line (1E15).

The second contaminant-depleted water transfer line (1E15) is connectedto the water tank (1E16) via a water input (1E18). In embodiments, thesecond contaminant-depleted water transfer line (1E15) has a watersupply valve (1E23) interposed in between the second water treatmentunit (1E11) and the water tank (1E16). In embodiments, the pressure dropacross the water supply valve (1E23) may range from: between about 1pound per square inch to about 5 pound per square inch; between about 5pound per square inch to about 10 pound per square inch; between about10 pound per square inch to about 15 pound per square inch; betweenabout 15 pound per square inch to about 20 pound per square inch;between about 25 pound per square inch to about 30 pound per squareinch; between about 35 pound per square inch to about 40 pound persquare inch; between about 45 pound per square inch to about 50 poundper square inch; between about 55 pound per square inch to about 60pound per square inch; between about 65 pound per square inch to about70 pound per square inch; between about 75 pound per square inch toabout 80 pound per square inch; between about 85 pound per square inchto about 90 pound per square inch; between about 95 pound per squareinch to about 100 pound per square inch; between about 100 pound persquare inch to about 125 pound per square inch; between about 125 poundper square inch to about 150 pound per square inch; or, between about150 pound per square inch to about 200 pound per square inch.

The water supply valve (1E23) has a controller (1E24) that is configuredto input and output a signal (1E25) to the computer (COMP). Inembodiments, a source of water (1E1) may be introduced to the interior(1E17) of the water tank (1E16) via a water supply line (1E19) and waterinput (1E18). The first water treatment unit (1E6) and second watertreatment unit (1E11) are optional because in many areas of the worldthe water quality is suitable for humans and animals to drink andingest.

The water tank (1E16) is equipped with a high-water level sensor (1E26)and a low water level sensor (1E28). The high-water level sensor (1E26)is configured to input a signal (1E27) to the computer (COMP) when thelevel reaches a pre-determined highest most vertical height in the watertank (1E16). The low water level sensor (1E28) is configured to input asignal (1E29) to the computer (COMP) when the level reaches apre-determined lowest most vertical height in the water tank (1E16).

A water supply pump (1E22) is connected to the water output (1E20) ofthe water tank (1E16) via a water discharge line (1E21). The watersupply pump (1E22) is configured to transfer water (1E1) from theinterior (1E17) of the water tank (1E16) to create a pressurized watersupply (1E32) that is routed for mixing to form an enhanced feedstockvia a pressurized water supply line (1E33).

A second water pressure sensor (1E30) is positioned on the discharge ofthe water supply pump (1E22) on the pressurized water supply line(1E33). The second water pressure sensor (1E30) is configured to input asignal (1E31) to the computer (COMP). A water flow sensor (1E34) ispositioned on the discharge of the water supply pump (1E22) on thepressurized water supply line (1E33). The water flow sensor (1E34) isconfigured to input a signal (1E35) to the computer (COMP).

A water control valve (1E36) with an integrated controller (1E37) ispositioned on the discharge of the water supply pump (1E22) on thepressurized water supply line (1E33). The controller (1E37) of the watercontrol valve (1E36) is configured to input and output signal (1E38) tothe computer (COMP). Water (1E1) routed through the water control valve(1E36) is then further routed towards being mixed to form an enhancedfeedstock via a water transfer line (1E41). A water quality sensor(1E42) is positioned on the water transfer line (1E41) and is configuredto input a signal (1E43) to the computer (COMP). A third water pressuresensor (1E39) is positioned on the water transfer line (1E41) and isconfigured to input a signal (1E40) to the computer (COMP).

The pressure drop across the water control valve (1E36) may range from:between about 1 pound per square inch to about 5 pound per square inch;between about 5 pound per square inch to about 10 pound per square inch;between about 10 pound per square inch to about 15 pound per squareinch; between about 15 pound per square inch to about 20 pound persquare inch; between about 25 pound per square inch to about 30 poundper square inch; between about 35 pound per square inch to about 40pound per square inch; between about 45 pound per square inch to about50 pound per square inch; between about 55 pound per square inch toabout 60 pound per square inch; between about 65 pound per square inchto about 70 pound per square inch; between about 75 pound per squareinch to about 80 pound per square inch; between about 85 pound persquare inch to about 90 pound per square inch; between about 95 poundper square inch to about 100 pound per square inch; between about 100pound per square inch to about 125 pound per square inch; between about125 pound per square inch to about 150 pound per square inch; or,between about 150 pound per square inch to about 200 pound per squareinch.

Enhancers (1E44) contained within the interior (1E46) of the enhancertank (1E45) may be routed to the interior (1E17) of the water tank(1E16) via an enhancer transfer line (1E48). The enhancer transfer line(1E48) is connected at one end to the enhancer tank (1E45) via anenhancer tank output (1E47) and at another end to the water tank (1E16)via an enhancer input (1E49). A water enhancer supply valve (1E52) withan integrated controller (1E53) is positioned on the enhancer transferline (1E48) and is configured to input and output a signal (1E54) to thecomputer (COMP). An enhancer flow sensor (1E50) is positioned on theenhancer transfer line (1E48) and is configured to input a signal (1E51)to the computer (COMP).

Feedstock (1A1), minerals (1B1), vitamins (1C1), polymer (1D1), andwater (1E1) are mixed to form an enhanced feedstock that is routed tothe interior (1F2) of the enhanced feedstock splitter (1F1) via anenhanced feedstock transfer line (1F0).

In embodiments, water may be added to the enhanced feedstock andtransferred to the feeding chamber so that the insect feeding chamberoperates at a water to insect ratio ranging from: between about 0.1 tonsof water per ton of insects produced to about 0.2 tons of water per tonof insects produced; between about 0.2 tons of water per ton of insectsproduced to about 0.4 tons of water per ton of insects produced; betweenabout 0.4 tons of water per ton of insects produced to about 0.6 tons ofwater per ton of insects produced; between about 0.6 tons of water perton of insects produced to about 0.8 tons of water per ton of insectsproduced; between about 0.8 tons of water per ton of insects produced toabout 1 ton of water per ton of insects produced; between about 1 ton ofwater per ton of insects produced to about 1.5 tons of water per ton ofinsects produced; between about 1.5 tons of water per ton of insectsproduced to about 2 tons of water per ton of insects produced; betweenabout 2 tons of water per ton of insects produced to about 3 tons ofwater per ton of insects produced; between about 3 tons of water per tonof insects produced to about 4 tons of water per ton of insectsproduced; between about 4 tons of water per ton of insects produced toabout 5 tons of water per ton of insects produced; between about 5 tonsof water per ton of insects produced to about 6 tons of water per ton ofinsects produced; between about 6 tons of water per ton of insectsproduced to about 7 tons of water per ton of insects produced; betweenabout 7 tons of water per ton of insects produced to about 8 tons ofwater per ton of insects produced; between about 8 tons of water per tonof insects produced to about 9 tons of water per ton of insectsproduced; between about 9 tons of water per ton of insects produced toabout 10 tons of water per ton of insects produced; between about 10tons of water per ton of insects produced to about 11 tons of water perton of insects produced; between about 11 tons of water per ton ofinsects produced to about 12 tons of water per ton of insects produced;between about 12 tons of water per ton of insects produced to about 13tons of water per ton of insects produced; between about 13 tons ofwater per ton of insects produced to about 14 tons of water per ton ofinsects produced; between about 14 tons of water per ton of insectsproduced to about 15 tons of water per ton of insects produced; betweenabout 15 tons of water per ton of insects produced to about 16 tons ofwater per ton of insects produced; between about 16 tons of water perton of insects produced to about 17 tons of water per ton of insectsproduced; between about 17 tons of water per ton of insects produced toabout 18 tons of water per ton of insects produced; between about 18tons of water per ton of insects produced to about 19 tons of water perton of insects produced; or, between about 19 tons of water per ton ofinsects produced to about 20 tons of water per ton of insects produced.

In embodiments, about 0.1 tons of water yields 1 ton of insects. Inembodiments, about 0.2 tons of water yields 1 ton of insects. Inembodiments, about 0.4 tons of water yields 1 ton of insects. Inembodiments, about 0.6 tons of water yields 1 ton of insects. Inembodiments, about 0.8 tons of water yields 1 ton of insects. Inembodiments, about 1 ton of water yields 1 ton of insects. Inembodiments, about 2 tons of water yields 1 ton of insects. Inembodiments, about 3 tons of water yields 1 ton of insects. Inembodiments, about 4 tons of water yields 1 ton of insects. Inembodiments, about 5 tons of water yields 1 ton of insects. Inembodiments, about 6 tons of water yields 1 ton of insects. Inembodiments, about 7 tons of water yields 1 ton of insects. Inembodiments, about 8 tons of water yields 1 ton of insects. Inembodiments, about 9 tons of water yields 1 ton of insects. Inembodiments, about 10 tons of water yields 1 ton of insects. Inembodiments, about 11 tons of water yields 1 ton of insects. Inembodiments, about 12 tons of water yields 1 ton of insects. Inembodiments, about 13 tons of water yields 1 ton of insects. Inembodiments, about 14 tons of water yields 1 ton of insects. Inembodiments, about 15 tons of water yields 1 ton of insects. Inembodiments, about 16 tons of water yields 1 ton of insects. Inembodiments, about 17 tons of water yields 1 ton of insects. Inembodiments, about 18 tons of water yields 1 ton of insects. Inembodiments, about 19 tons of water yields 1 ton of insects. Inembodiments, about 20 tons of water yields 1 ton of insects.

Enhanced Feedstock Distribution Module (1F)

The enhanced feedstock splitter (1F1) has an interior (1F2), a splitterinput (1F3), a first output (1F10), second output (1F15), and a thirdoutput (1F20). The enhanced feedstock splitter (1F1) is configured tomix the feedstock (1A1), minerals (1B1), vitamins (1C1), polymer (1D1),and water (1E1) and to split the mixed enhanced feedstock into aplurality of streams including a first enhanced feedstock stream (EF1),second enhanced feedstock stream (EF2), and a third enhanced feedstockstream (EF3). Each of the first enhanced feedstock stream (EF1), secondenhanced feedstock stream (EF2), and third enhanced feedstock stream(EF3), may be transferred each to a first feeding chamber (FC1), secondfeeding chamber (FC2), and third feeding chamber (FC3), respectively.

An enhanced feedstock moisture sensor (1A12B) is positioned on theenhanced feedstock transfer line (1F0) and is configured to input asignal (1A13B) to the computer (COMP). The enhanced feedstock moisturesensor (1A12B) may be used to gauge the amount of moisture within theenhanced feedstock to increase or decrease the flow of water (1E1)passed through the water flow sensor (1E34) and water control valve(1E36).

The enhanced feedstock splitter (1F1) has a top section (1F4), bottomsection (1F5), and at least one side wall (1F6). The enhanced feedstocksplitter (1F1) may be cylindrical or rectangular or any otherconceivable shape so long as it outputs at least one first enhancedfeedstock stream. In embodiments, the enhanced feedstock splitter (1F1)has a splitter input (1F3) positioned on the top section (1F4).

In embodiments, the enhanced feedstock splitter (1F1) has a splitterfirst screw conveyor (1F9), splitter second screw conveyor (1F14), andsplitter third screw conveyor (1F19) positioned on the bottom section(1F5). In embodiments, a first splitter level sensor (1F7) is positionedon the side wall (1F6) of the enhanced feedstock splitter (1F1) which isconfigured to input a signal (1F8) to the computer (COMP).

The splitter first screw conveyor (1F9) has a first output (1F10) and isconfigured to discharge a first enhanced feedstock stream (EF1) to afirst feeding chamber (FC1). The splitter first screw conveyor (1F9) isequipped with a splitter first screw conveyor motor (1F11) andintegrated controller (1F12) that is configured to input and output asignal (1F13) to the computer (COMP).

A first weigh screw (1F24) is positioned on the first output (1F10) ofthe splitter first screw conveyor (1F9). The first weigh screw (1F24)has a first weigh screw input (1F25) and a first weigh screw output(1F26), with an integrated mass sensor (1F27) that is configured toinput a signal (1F28) to the computer (COMP). The first weigh screw(1F24) has a first weigh screw motor (1F29) with an integratedcontroller (1F30) that is configured to input and output a signal (1F31)to the computer (COMP). A first weighed enhanced feedstock stream (1F32)or a first enhanced feedstock stream (EF1) is discharged from the firstweigh screw output (1F26).

The splitter second screw conveyor (1F14) has a first output (1F10) andis configured to discharge a second enhanced feedstock stream (EF2) to asecond feeding chamber (FC2). The splitter second screw conveyor (1F14)is equipped with a splitter second screw conveyor motor (1F16) andintegrated controller (1F17) that is configured to input and output asignal (1F18) to the computer (COMP). A second weigh screw (1F33) ispositioned on the second output (1F15) of the splitter second screwconveyor (1F14). The second weigh screw (1F33) has a second weigh screwinput (1F34) and a second weigh screw output (1F35), with an integratedmass sensor (1F26) that is configured to input a signal (1F37) to thecomputer (COMP). The second weigh screw (1F33) has a second weigh screwmotor (1F38) with an integrated controller (1F39) that is configured toinput and output a signal (1F40) to the computer (COMP). A secondweighed enhanced feedstock stream (1F41) or a second enhanced feedstockstream (EF2) is discharged from the second weigh screw output (1F35).

The splitter third screw conveyor (1F19) has a first output (1F10) andis configured to third enhanced feedstock stream (EF3) to a thirdfeeding chamber (FC3). The splitter third screw conveyor (1F19) isequipped with a splitter third screw conveyor motor (1F21) andintegrated controller (1F22) that is configured to input and output asignal (1F23) to the computer (COMP). A third weigh screw (1F42) ispositioned on the third output (1F20) of the splitter third screwconveyor (1F19). The third weigh screw (1F42) has a third weigh screwinput (1F43) and a third weigh screw output (1F44), with an integratedmass sensor (1F45) that is configured to input a signal (1F46) to thecomputer (COMP). The third weigh screw (1F42) has a third weigh screwmotor (1F47) with an integrated controller (1F48) that is configured toinput and output a signal (1F49) to the computer (COMP). A third weighedenhanced feedstock stream (1F50) or a third enhanced feedstock stream(EF3) is discharged from the third weigh screw output (1F44).

FIG. 3:

FIG. 3 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein the egg transfer system (244) of theinsect feeding module (2000) is at a first state in a first retractedheight (H1).

A first weighed enhanced feedstock stream (1F32), or otherwise termed afirst enhanced feedstock stream (EF1), is shown in FIG. 3 to beintroduced to a first feeding chamber (FC1) of an insect feeding module(2000) via an enhanced feedstock input (206). The non-limitingdescription of the insect feeding module (2000) shown in FIG. 3 includesa feeding chamber (200). In embodiments, the feeding chamber (200) inFIG. 3 is a first feeding chamber (FC1) in an Insect ProductionSuperstructure System (IPSS) that includes a plurality of insect feedingchambers (FC1, FC2, FC3). The insect feeding module (2000) is shown tobe in fluid communication with an insect evacuation module (3000). Thefeeding chamber (200) contained within an insect feeding module (2000)of FIG. 3 is shown to be in fluid communication with a separator (300)contained within an insect evacuation module (3000).

The feeding chamber (200) of is shown to have an interior (201) definedby at least one side wall (202). Each side wall (202) of the embodimentof FIG. 3 is shown to have perforations as to be comprised of a mesh, ora screen, or the like. However, it is to be noted that any such wall,perforated or not perforated, screen or an impermeable surface shallsuffice. It is also to be noted that the side wall (202) when made up ofa screen-type material has opening that are lesser in size than theinsects contained within the interior (201) of the feeding chamber(200).

In embodiments, the feeding chamber (200) has both a top (203) and abottom (204). In the embodiment of FIG. 3, the top and bottom are bothmade up of a permeable metal or plastic or wire mesh or the like.However, in some embodiments, there is no bottom (204) at all, or thebottom is made up of a plurality of slats as described below. The firstweighed enhanced feedstock stream (1F32), or otherwise termed a firstenhanced feedstock stream (EF1), is introduced to an enhanced feedstockdistributor (207) positioned within the interior (201) of the feedingchamber (200).

The feeding chamber is equipped with a humidity sensor (208) that isconfigured to measure the humidity within the interior (201) and input asignal (209) to the computer (COMP). The feeding chamber is equippedwith a first temperature sensor (210) that is configured to measure thetemperature of a first region within the interior (201) and input asignal (211) to the computer (COMP). The feeding chamber is equippedwith a second temperature sensor (212) that is configured to measure thetemperature of a first region within the interior (201) and input asignal (213) to the computer (COMP).

A network (220) of cells (219) are positioned within the interior (201)of the feeding chamber and are configured to permit insects (225) toreside therein. FIG. 4 shows one non-limiting embodiment of a network(220) of cells (219) for growing insects within a feeding chamber (200)of the insect feeding module (2000) shown in FIG. 3. The network (220)of cells (219) has openings (222) positioned at a first end (221) andopenings (224) positioned at a second end (223). Insects (225) mayreside in the passageways between the openings (222) at the first end(221) and the openings (224) at the second end (223). The cells (219)have a cell length (C-L) and a cell width (C-W). The network (220) ofcells (219) has a network length (N-L) and a network width (N-W). Inembodiments, the network (220) of cells (219) has a network length (N-L)that is greater than the network width (N-W). In embodiments, thenetwork (220) of cells (219) has a network length (N-L) that is lessthan the network width (N-W). The cell width (C-W) is greater than thewidth (1 i-W) of a first insect (1 i) that resides within the interior(201) of the feeding chamber (200). The cell width (C-W) is greater thanthe average insect width (Ni-W) of a Nth insect (Ni) that collectivelyreside within the interior (201) of the feeding chamber (200). The celllength (C-L) is greater than the length (2 i-L) of a first insect (1 i)that resides within the interior (201) of the feeding chamber (200). Thecell length (C-L) is greater than the average insect length (Ni-LW) of aNth insect (Ni) that collectively reside within the interior (201) ofthe feeding chamber (200).

Obviously, many insects (225) may be present within the feeding chamber(200) at any given time. In embodiments, the throughput of insects (225)includes one or more throughputs selected from the group consisting of:0.1 pounds per day to 0.2 pounds per day, 0.2 pounds per day to 0.4pounds per day, 0.4 pounds per day to 0.8 pounds per day, 0.8 pounds perday to 1.0 pounds per day, 1 pounds per day to 2 pounds per day, 2pounds per day to 4 pounds per day, 4 pounds per day to 8 pounds perday, 8 pounds per day to 16 pounds per day, 16 pounds per day to 32pounds per day, 32 pounds per day to 64 pounds per day, 64 pounds perday to 128 pounds per day, 128 pounds per day to 256 pounds per day, 256pounds per day to 512 pounds per day, 512 pounds per day to 1024 poundsper day, 1024 pounds per day to 2048 pounds per day, 2048 pounds per dayto 4096 pounds per day, 4096 pounds per day to 8192 pounds per day, 8192pounds per day to 16384 pounds per day, 16384 pounds per day to 32768pounds per day, 32768 pounds per day to 65536 pounds per day, 65536pounds per day to 131072 pounds per day, 131072 pounds per day to 262144pounds per day, 262144 pounds per day to 524288 pounds per day, 524288pounds per day to 1048576 pounds per day, 1048576 pounds per day to2097152 pounds per day, and 2097152 pounds per day to 4194304 pounds perday.

In embodiments, the insect production superstructure system producesinsects at a throughput ranging from one or more selected from the groupconsisting of 0.1 tons per day (TPD) to 0.2 TPD, 0.2 TPD to 0.4 TPD, 0.4TPD to 0.8 TPD, 0.8 TPD to 1 TPD, 1 TPD to 1.25 TPD, 1.25 TPD to 2.5TPD, 2.5 TPD to 3 TPD, 3 TPD to 3.5 TPD, 3.5 TPD to 4 TPD, 4 TPD to 4.5TPD, 4.5 TPD to 5 TPD, 5 TPD to 5.5 TPD, 5.5 TPD to 6 TPD, 6 TPD to 6.5TPD, 6.5 TPD to 7 TPD, 7 TPD to 7.5 TPD, 7.5 TPD to 8 TPD, 8 TPD to 8.5TPD, 8.5 TPD to 9 TPD, 9 TPD to 9.5 TPD, 9.5 TPD to 10 TPD, 10 TPD to 15TPD, 15 TPD to 20 TPD, 20 TPD to 25 TPD, 25 TPD to 50 TPD, 50 TPD to 75TPD, 75 TPD to 100 TPD, 100 TPD to 200 TPD, 200 TPD to 300 TPD, 300 TPDto 400 TPD, 400 TPD to 500 TPD, 500 TPD to 1000 TPD, 1000 TPD to 1500TPD, 1500 TPD to 2000 TPD, 2000 TPD to 2500 TPD, or 2500 TPD to 3000TPD.

This may include: a first insect (1 i) having a first insect length (1i-L), a first insect width (1 i-W), and a first insect mass (1 i-WT); asecond insect (2 i) having a second insect length (2 i-L), a secondinsect width (2 i-W), and a second insect mass (2 i-WT); and a Nthinsect (Ni) that has an average insect length (Ni-L), an average insectwidth (Ni-W), and an average insect mass (Ni-WT). The average insectlength (Ni-L) is the sum of the first insect length (1 i-L) and thesecond insect length (2 i-L) divided by the number of insects that beingtwo in this particular instance and embodiment. The average insect width(Ni-W) is the sum of the first insect width (1 i-W) and the secondinsect width (2 i-W) divided by the number of insects that being two inthis particular instance and embodiment. It is of course obvious to oneof ordinary skill in the art that more than two insects (225, 1 i, 2 i)are contained within the interior (201) of the feeding chamber (200) andthat both the average insect length (Ni-L) and average insect width(Ni-W) are averaged over a plurality of insects.

In embodiments, the cell width (C-W) ranges from: between about 0.125inches to about 0.25 inches; between about 0.25 inches to about 0.50inches; between about 0.5 inches to about 0.75 inches; between about0.75 inches to about 1 inch; between about 1 inch to about 1.25 inches;between about 1.25 inch to about 1.50 inches; between about 1.50 inchesto about 1.75 inches; between about 1.75 inches to about 2 inches;between about 2 inches to about 2.25 inches; between about 2.25 inchesto about 2.50 inches; between about 2.50 inches to about 2.75 inches;between about 2.75 inches to about 2.75 inches; between about 2.75inches to about 3 inches; between about 3 inches to about 3.25 inches;between about 3.25 inch to about 3.50 inches; between about 3.50 inchesto about 3.75 inches; between about 3.75 inches to about 4 inches;between about 4 inches to about 4.25 inches; between about 4.25 inch toabout 4.50 inches; between about 4.50 inches to about 4.75 inches; and,between about 4.75 inches to about 5 inches.

In embodiments, the cell length (C-L) ranges from: between about 0.5feet to about 1 foot; between about 1 feet to about 2 feet; betweenabout 2 feet to about 3 feet; between about 3 feet to about 4 feet;between about 4 feet to about 5 feet; between about 5 feet to about 6feet; between about 6 feet to about 7 feet; between about 7 feet toabout 8 feet; between about 8 feet to about 9 feet; between about 9 feetto about 10 feet; between about 10 feet to about 11 feet; between about11 feet to about 12 feet; between about 12 feet to about 13 feet;between about 13 feet to about 14 feet; between about 14 feet to about15 feet; between about 15 feet to about 16 feet; between about 16 feetto about 17 feet; between about 17 feet to about 18 feet; between about18 feet to about 19 feet; between about 19 feet to about 20 feet;between about 20 feet to about 21 feet; between about 21 feet to about22 feet; between about 22 feet to about 23 feet; between about 23 feetto about 24 feet; between about 24 feet to about 25 feet; between about25 feet to about 26 feet; between about 26 feet to about 27 feet;between about 27 feet to about 28 feet; between about 28 feet to about29 feet; between about 29 feet to about 30 feet; between about 30 feetto about 31 feet; between about 31 feet to about 32 feet; between about32 feet to about 33 feet; between about 33 feet to about 34 feet;between about 34 feet to about 35 feet; between about 35 feet to about36 feet; between about 36 feet to about 37 feet; between about 37 feetto about 38 feet; between about 38 feet to about 39 feet; and, betweenabout 39 feet to about 40 feet.

In embodiments, the average insect width (Ni-W) ranges from: betweenabout 0.005 inches to 0.015625 inches, 0.015625 inches to about 0.03125inches; between about 0.03125 inches to about 0.0625 inches; betweenabout 0.0625 inches to about 0.125 inches; between about 0.125 inches toabout 0.25 inches; between about 0.25 inches to about 0.50 inches;between about 0.5 inches to about 0.75 inches; between about 0.75 inchesto about 1 inch; between about 1 inch to about 1.25 inches; betweenabout 1.25 inch to about 1.50 inches; between about 1.50 inches to about1.75 inches; between about 1.75 inches to about 2 inches; between about2 inches to about 2.25 inches; between about 2.25 inches to about 2.50inches; between about 2.50 inches to about 2.75 inches; between about2.75 inches to about 2.75 inches; and, between about 2.75 inches toabout 3 inches.

In embodiments, the average insect length (Ni-L) ranges from: betweenabout 0.01 inches to 0.05 inches, 0.05 inches to 0.075 inches, 0.075inches to 0.1 inches, 0.1 inch to 0.125 inches, 0.125 inches to about0.25 inches; between about 0.25 inches to about 0.50 inches; betweenabout 0.5 inches to about 0.75 inches; between about 0.75 inches toabout 1 inch; between about 1 inch to about 1.25 inches; between about1.25 inch to about 1.50 inches; between about 1.50 inches to about 1.75inches; between about 1.75 inches to about 2 inches; between about 2inches to about 2.25 inches; between about 2.25 inches to about 2.50inches; between about 2.50 inches to about 2.75 inches; between about2.75 inches to about 2.75 inches; between about 2.75 inches to about 3inches; between about 3 inches to about 3.25 inches; between about 3.25inch to about 3.50 inches; between about 3.50 inches to about 3.75inches; between about 3.75 inches to about 4 inches; between about 4inches to about 4.25 inches; between about 4.25 inch to about 4.50inches; between about 4.50 inches to about 4.75 inches; between about4.75 inches to about 5 inches; between about 5 inches to about 5.25inches; between about 5.25 inches to about 5.5 inches; between about 5.5inches to about 5.75 inches; between about 5.75 inches to about 6inches; between about 6 inches to about 7 inches; between about 7 inchesto about 8 inches; between about 8 inches to about 9 inches; and,between about 9 inches to about 10 inches.

Referring again to FIG. 3, a vibration unit (214) may be connected tothe network (220) of cells (219) at a first vibration unit connection(218A) and a second vibration unit connection (218B). The vibration unit(214) is equipped with a vibration unit motor (215) and integratedcontroller (216) that is configured to input and output a signal (217)to the computer (COMP). The vibration unit (214) is used to shake or toprovide oscillations to occur within the network (220) of cells (219) todislodge insects (225) from within the passageway between the first end(221) openings (222) and the second end (223) openings (224).Alternately, the vibration unit (214) may vibrate the entire feedingchamber (200) or at least a portion of the feeding chamber (200) so asto effectuate disclosing insects (225) from their resting surface withinthe network (220) of cells (219) in between the first end (221) openings(222) and the second end (223) openings (224).

In embodiments, a cell network differential pressure sensor (226) may beinstalled to measure to pressure across the network (220) of cells (219)to ascertain some measure of the mass or volume or quantity of insectsthat reside in between the first end (221) openings (222) and the secondend (223) openings (224).

The cell network differential pressure sensor (226) is configured toinput a signal (227) to the computer (COMP). When a pre-determineddifferential pressure is measured across the feeding chamber (200),insects may be evacuated therefrom. In embodiments, the pre-determineddifferential pressure across the feeding chamber (200) ranges from:about 0.015625 inches of water to about 0.03125 inches of water; betweenabout 0.03125 inches of water to about 0.0625 inches of water; betweenabout 0.0625 inches of water to about 0.125 inches of water; betweenabout 0.125 inches of water to about 0.25 inches of water; between about0.25 inches of water to about 0.50 inches of water; between about 0.5inches of water to about 0.75 inches of water; between about 0.75 inchesof water to about 1 inch; between about 1 inch to about 1.25 inches ofwater; between about 1.25 inch to about 1.50 inches of water; betweenabout 1.50 inches of water to about 1.75 inches of water; between about1.75 inches of water to about 2 inches of water; between about 2 inchesof water to about 2.25 inches of water; between about 2.25 inches ofwater to about 2.50 inches of water; between about 2.50 inches of waterto about 2.75 inches of water; between about 2.75 inches of water toabout 2.75 inches of water; between about 2.75 inches of water to about3 inches of water; between about 3 inches of water to about 3.25 inchesof water; between about 3.25 inch to about 3.50 inches of water; betweenabout 3.50 inches of water to about 3.75 inches of water; between about3.75 inches of water to about 4 inches of water; between about 4 inchesof water to about 4.25 inches of water; between about 4.25 inch to about4.50 inches of water; between about 4.50 inches of water to about 4.75inches of water; between about 4.75 inches of water to about 5 inches ofwater; between about 5 inches of water to about 5.25 inches of water;between about 5.25 inches of water to about 5.5 inches of water; betweenabout 5.5 inches of water to about 5.75 inches of water; between about5.75 inches of water to about 6 inches of water; between about 6 inchesof water to about 7 inches of water; between about 7 inches of water toabout 8 inches of water; between about 8 inches of water to about 9inches of water; between about 10 inches of water to about 15 inches ofwater; between about 15 inches of water to about 20 inches of water;between about 20 inches of water to about 25 inches of water; betweenabout 25 inches of water to about 30 inches of water; between about 30inches of water to about 35 inches of water; between about 35 inches ofwater to about 40 inches of water; between about 40 inches of water toabout 45 inches of water; between about 45 inches of water to about 50inches of water; between about 50 inches of water to about 55 inches ofwater; between about 55 inches of water to about 60 inches of water;between about 60 inches of water to about 65 inches of water; betweenabout 65 inches of water to about 70 inches of water; between about 70inches of water to about 75 inches of water; between about 75 inches ofwater to about 80 inches of water; between about 80 inches of water toabout 85 inches of water; between about 85 inches of water to about 90inches of water; between about 90 inches of water to about 95 inches ofwater; and, between about 95 inches of water to about 100 inches ofwater.

The cell network differential pressure sensor (226) is connected to theinterior (201) of the feeding chamber (200) by a first end impulse line(228) with a first end impulse line connection (232) and a second endimpulse line (233) with a second end impulse line connection (237). FIG.3 shows the first end impulse line (228) connected to the feedingchamber (200) via a first end impulse line connection (232) that ispositioned vertically above the first end (221) openings (222) of thenetwork (220) of cells (219). FIG. 3 also shows the second end impulseline (233) connected to the feeding chamber (200) via a second endimpulse line connection (237) that is positioned vertically below thesecond end (223) openings (224) of the network (220) of cells (219).

The first end impulse line (228) and second end impulse line (233) arepreferably tubes ranging from ⅛″, ¼″, ⅜″, ½″, ¾″, or 1″ stainless steel,plastic, polymer, metal tubing or piping. To prevent insects (225) fromcrawling up the first end impulse line (228), or to prevent clogging ofparticulates, and thus preventing the cell network differential pressuresensor (226) from accurately measuring differential pressure across thenetwork (220) of cells (219), a first impulse line gas supply (231) maybe provided to apply a continuous purge or gas, such as air, or CO2, orthe like. The first impulse line gas supply (231) is controlled and setto a pre-determined flow rate by adjusting a first air purge flowregulator (230) wherein the flow rate is detected via a first air purgeflow sensor (229). Similarly, to prevent insects (225) from crawling upthe second end impulse line (233), or to prevent clogging ofparticulates, and thus preventing the cell network differential pressuresensor (226) from accurately measuring differential pressure across thenetwork (220) of cells (219), a second impulse line gas supply (236) maybe provided to apply a continuous purge or gas, such as air, or CO2, orthe like. The second impulse line gas supply (236) is controlled and setto a pre-determined flow rate by adjusting a second air purge flowregulator (235) wherein the flow rate is detected via a second air purgeflow sensor (234).

In embodiments, a gas quality sensor (GC1) is configured to analyze thegas quality within the interior (201) of the feeding chamber (200). Inembodiments, the gas quality sensor (GC1) is equipped to send a signal(XGC1) to the computer (COMP). In embodiments, the gas quality sensor(GC1) is comprised of one or more analyzers selected from the groupconsisting of Fourier-transform infrared spectroscopy, gaschromatography, mass spectrometry, and ultra-high performance liquidchromatography.

In embodiments, the interior (201) of the feeding chamber (200) ismaintained at a predetermined concentration of ammonia, methane, urea,carbon dioxide. In response to the signal (XGC1) from the gas qualitysensor (GC1) the computer (COMP) instructs the insect evacuation fan(312) to pull a vacuum on the interior (201) of the feeding chamber(200) is maintained at a predetermined concentration of ammonia,methane, urea, carbon dioxide.

In other embodiments, in response to the signal (XGC1) from the gasquality sensor (GC1) the computer (COMP) instructs the air supply fan(271) to delivery an air supply (262) to the interior (201) of thefeeding chamber (200) to maintain the interior (201) of the feedingchamber (200) at a predetermined concentration of ammonia, methane,carbon dioxide, hydrogen sulfide.

In embodiments, the predetermined concentration of ammonia within theinterior (201) of the feeding chamber (200) ranges from: 0.05 parts permillion (ppm) to 0.1 ppm, 0.1 ppm to 0.2 ppm, 0.2 ppm to 0.4 ppm, 0.4ppm to 0.8 ppm, 0.8 ppm to 1 ppm, 1 ppm to 2 ppm, 2 ppm to 3 ppm, 3 ppmto 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8 ppm, 8 ppm to 9ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 25 ppm, 25 ppm to 50ppm, and 50 ppm to 100 ppm.

In embodiments, the predetermined concentration of methane within theinterior (201) of the feeding chamber (200) ranges from: 0.05 parts permillion (ppm) to 0.1 ppm, 0.1 ppm to 0.2 ppm, 0.2 ppm to 0.4 ppm, 0.4ppm to 0.8 ppm, 0.8 ppm to 1 ppm, 1 ppm to 2 ppm, 2 ppm to 3 ppm, 3 ppmto 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8 ppm, 8 ppm to 9ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 25 ppm, 25 ppm to 50ppm, and 50 ppm to 100 ppm.

In embodiments, the predetermined concentration of carbon dioxide withinthe interior (201) of the feeding chamber (200) ranges from: 390 partsper million (ppm) to 400 ppm, 400 ppm to 410 ppm, 410 ppm to 420 ppm,420 ppm to 430 ppm, 430 ppm to 440 ppm, 440 ppm to 450 ppm, 450 ppm to460 ppm, 460 ppm to 470 ppm, 470 ppm to 480 ppm, 480 ppm to 490 ppm, 490ppm to 500 ppm, 500 ppm to 600 ppm, 600 ppm to 700 ppm, 700 ppm to 800ppm, 800 ppm to 900 ppm, 900 ppm to 1000 ppm, 1000 ppm to 2000 ppm, 2000ppm to 3000 ppm, 3000 ppm to 4000 ppm, 4000 ppm to 5000 ppm, 5000 ppm to6000 ppm, 6000 ppm to 7000 ppm, 7000 ppm to 8000 ppm, 8000 ppm to 9000ppm, and 9000 ppm to 10000 ppm.

In embodiments, the predetermined concentration of hydrogen sulfidewithin the interior (201) of the feeding chamber (200) ranges from: 0.05parts per million (ppm) to 0.1 ppm, 0.1 ppm to 0.2 ppm, 0.2 ppm to 0.4ppm, 0.4 ppm to 0.8 ppm, 0.8 ppm to 1 ppm, 1 ppm to 2 ppm, 2 ppm to 3ppm, 3 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8 ppm, 8ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 25 ppm, 25ppm to 50 ppm, and 50 ppm to 100 ppm. In embodiments, a decibel meter(DM1) is configured to analyze noise or sound levels by measuring soundpressure level (in decibel (dB)) within the interior (201) of thefeeding chamber (200). In embodiments, the gas quality sensor (GC1) isequipped to send a signal (XGC1) to the computer (COMP). In embodiments,the decibel meter (DM1) indicates a range of sound pressure in decibels(dB) including one or more decibel ranges selected from the groupconsisting of: 86 decibels (dB) to 88 dB, 88 dB to 90 dB, 90 dB to 92dB, 92 dB to 94 dB, 94 dB to 96 dB, 96 dB to 98 dB, 98 dB to 100 dB, 100dB to 102 dB, 102 dB to 104 dB, 104 dB to 106 dB, 106 dB to 108 dB, or108 dB to 110 dB.

In embodiments, a sound damping system (SDS) is configured to reduce thenoise or sound levels by reducing the sound pressure level (in decibel(dB)) within the interior (201) of the feeding chamber (200) to apredetermined decibel range selected from the group consisting of: 86decibels (dB) to 88 dB, 88 dB to 90 dB, 90 dB to 92 dB, 92 dB to 94 dB,94 dB to 96 dB, 96 dB to 98 dB, 98 dB to 100 dB, 100 dB to 102 dB, 102dB to 104 dB, 104 dB to 106 dB, 106 dB to 108 dB, or 108 dB to 110 dB.

In embodiments, a sound damping system (SDS) is configured to reduce thenoise or sound levels by reducing the sound pressure level (in decibel(dB)) within the interior (201) of the feeding chamber (200) by apercentage including one or more percentage ranges selected from thegroup consisting of: 5 percent to 10 percent, 10 percent to 15 percent,15 percent to 20 percent, 20 percent to 25 percent, 25 percent to 30percent, 30 percent to 35 percent, 35 percent to 40 percent, 40 percentto 45 percent, 45 percent to 50 percent, 50 percent to 55 percent, 55percent to 60 percent, 60 percent to 65 percent, 65 percent to 70percent, 70 percent to 75 percent, 75 percent to 80 percent, 80 percentto 85 percent, 85 percent to 90 percent, 90 percent to 95 percent, or 95percent to 100 percent.

In embodiments, a sound damping system (SDS) includes a means ofreducing the sound pressure within the interior (201) of the feedingchamber (200) including one or more selected from the group consistingof: using noise barriers to reflect or absorb the energy of the soundwaves, using damping structures such as sound baffles, or using activeantinoise sound generators, sound absorption damping, sound redirectiondamping, porous absorbers, open cell rubber foams which absorb noise byfriction within the cell structure, melamine sponges which absorb noiseby friction within the cell structure, resonant panels, refection, anddiffusion.

In embodiments, a sound damping system (SDS) includes a means ofreducing the sound pressure within the interior (201) of the feedingchamber (200) including one or more selected from the group consistingof: acoustic board, acoustic foam, acoustic quieting, noise barrier,noise mitigation, sound masking, and damping.

An air input (260) is configured to permit an air supply (262) to betransferred to the interior (201) of the feeding chamber (200) via anair supply entry conduit (261). An optional inlet gas distributor (263)may be positioned at the interface of the air input (260) so as tosubstantially uniformly distribute the air supply (262) over thecross-section of the interior (201) of the feeding chamber (200). Inembodiments, the inlet gas distributor (263) may serve to effectuate ahigh velocity blast of air to the openings (222, 224) of the network(220) of cells (219) to aide in dislodging insects (225) from the cells(219) and to permit substantially complete evacuation of the egg-layinginsects (225) present thing the interior (201) of the feeding chamber(200).

FIG. 3 shows an air supply fan (271) connected to the interior (201) ofthe feeding chamber (200) via the air supply entry conduit (261). Theair supply fan (271) equipped with an air supply fan motor (272) andcontroller (273) is configured to input and output a signal (274) to thecomputer (COMP). An air heater (264) may be interposed in the air supplyentry conduit (261) in between the air supply fan (271) and the feedingchamber (200).

Water (275) in the form of liquid or vapor may be introduced to the airsupply entry conduit (261) via a water transfer line (276). A waterinput valve (278), and a water flow sensor (279) may also be installedon the water transfer line (276). The water flow sensor (279) isconfigured to input a signal (280) to the computer (COMP). The airsupply (262) may be mixed with the water (275) in a water and gas mixingsection (281) of the air supply entry conduit (261). FIG. 1 shows thewater and gas mixing section (281) upstream of the air heater (264) butit may alternately also be placed downstream.

The air heater (264) may be electric, operated by natural gas,combustion, solar energy, alternative energy, or it may be a heattransfer device that uses a working heat transfer medium, such as steamor any other heat transfer medium known to persons having an ordinaryskill in the art to which it pertains. FIG. 3 shows the air heater (264)to have a heat transfer medium input (265) and a heat transfer mediumoutput (266). In embodiments, a first steam supply (LCL) is provided tothe heat transfer medium input (265). In embodiments, the first steamsupply (LCL) is provided from FIG. 14L.

In embodiments, heat transfer medium input (265) of the air heater (264)is equipped with a heat exchanger heat transfer medium inlet temperature(T3) that is configured to input a signal (XT3) to the computer (COMP).In embodiments, heat transfer medium output (266) of the air heater(264) is equipped with a heat exchanger heat transfer medium outlettemperature (T4) that is configured to input a signal (XT4) to thecomputer (COMP). In embodiments, a first condensate (LAQ) is dischargedfrom the heat transfer medium output (266) and is provided to thecondensate tank (LAP) on FIG. 14L.

A first humidity sensor (267) is positioned on the discharge of the airsupply fan (271) upstream of the water and gas mixing section (281). Thefirst humidity sensor (267) is configured to input a signal (268) to thecomputer (COMP). A heat exchanger inlet gas temperature sensor (T1) ispositioned on the discharge of the air supply fan (271) upstream of theair heater (264). The heat exchanger inlet gas temperature sensor (T1)is configured to input a signal (XT1) to the computer (COMP).

A second humidity sensor (269) is positioned on the discharge of the airheater (264) upstream of the air input (260) to the interior (201) ofthe feeding chamber (200). The second humidity sensor (266) isconfigured to input a signal (270) to the computer (COMP). A heatexchanger outlet gas temperature sensor (T2) is positioned on thedischarge of the air heater (264) upstream of the air input (260) to theinterior (201) of the feeding chamber (200). The heat exchanger outletgas temperature sensor (T2) is configured to input a signal (XT2) to thecomputer (COMP).

In embodiments, the air supply fan (271), air heater (264), and airsupply (262), permit the computer automation while integrated with theheat exchanger inlet gas temperature sensor (T1), heat exchanger outletgas temperature sensor (T2), and feeding chamber (200) temperaturesensors (210, 212), to operate under a wide variety of automatedtemperature operating conditions including varying the temperature rangein the feeding chamber (200) from: below 32 degrees Fahrenheit, betweenabout 32 degrees Fahrenheit to about 40 degrees Fahrenheit; betweenabout 40 degrees Fahrenheit to about 45 degrees Fahrenheit; betweenabout 45 degrees Fahrenheit to about 50 degrees Fahrenheit; betweenabout 50 degrees Fahrenheit to about 55 degrees Fahrenheit; betweenabout 55 degrees Fahrenheit to about 60 degrees Fahrenheit; betweenabout 60 degrees Fahrenheit to about 65 degrees Fahrenheit; betweenabout 65 degrees Fahrenheit to about 70 degrees Fahrenheit; betweenabout 70 degrees Fahrenheit to about 75 degrees Fahrenheit; betweenabout 75 degrees Fahrenheit to about 80 degrees Fahrenheit; betweenabout 80 degrees Fahrenheit to about 85 degrees Fahrenheit; betweenabout 85 degrees Fahrenheit to about 90 degrees Fahrenheit; betweenabout 90 degrees Fahrenheit to about 95 degrees Fahrenheit; betweenabout 95 degrees Fahrenheit to about 100 degrees Fahrenheit; betweenabout 100 degrees Fahrenheit to about 105 degrees Fahrenheit; betweenabout 105 degrees Fahrenheit to about 110 degrees Fahrenheit; betweenabout 110 degrees Fahrenheit to about 115 degrees Fahrenheit; and,between about 115 degrees Fahrenheit to about 120 degrees Fahrenheit.

In embodiments, the air supply fan (271), air heater (264), air supply(262), and water (275) permit the computer automation while integratedwith the first humidity sensor (267), second humidity sensor (269), andfeeding chamber (200) humidity sensor (208), to operate under a widevariety of automated operating humidity conditions including varying thehumidity range in the feeding chamber (200) from: between about 5percent humidity to about 10 percent humidity; between about 10 percenthumidity to about 15 percent humidity; between about 15 percent humidityto about 20 percent humidity; between about 20 percent humidity to about25 percent humidity; between about 25 percent humidity to about 30percent humidity; between about 30 percent humidity to about 35 percenthumidity; between about 35 percent humidity to about 40 percenthumidity; between about 40 percent humidity to about 45 percenthumidity; between about 45 percent humidity to about 50 percenthumidity; between about 50 percent humidity to about 55 percenthumidity; between about 55 percent humidity to about 60 percenthumidity; between about 60 percent humidity to about 65 percenthumidity; between about 65 percent humidity to about 70 percenthumidity; between about 70 percent humidity to about 75 percenthumidity; between about 75 percent humidity to about 80 percenthumidity; between about 80 percent humidity to about 85 percenthumidity; between about 85 percent humidity to about 90 percenthumidity; between about 90 percent humidity to about 95 percenthumidity; and, between about 95 percent humidity to about 100 percenthumidity.

FIG. 3 shows the feeding chamber (200) connected to a separator (300)via a feeding chamber exit conduit (302). The insect evacuation module(3000) shown in FIG. 3 only contains a first separator (S1), however itis to be noted that more than one separator (S2, S3) may be utilized insome circumstances.

The feeding chamber exit conduit (302) is connected at a first end tothe feeding chamber (200) via an insect evacuation output (205) andconnected at another end to a separator (300) via an insect and gasmixture input (303). The feeding chamber exit conduit (302) isconfigured to transfer an insect and gas mixture (304) from the feedingchamber (200) to the separator (300).

The insect and gas mixture (304) has an insect portion (304A) and a gasportion (304B). The gas portion is mostly air, however may contain someCO2 if some CO2 is used in the first impulse line gas supply (231) orthe second impulse line gas supply (236). The separator (300), showingin FIG. 3 as a first separator (S1), is also shown in a filter. However,in other embodiments, the first separator (S1) may be a filter, acyclone, or any other conceivable means to achieve the end of separatinginsects from a gas.

The separator (300) of FIG. 3 is a filter and contains an interior(301), an entry section (305) and an exit section (307). A filterelement (306) separates the entry section (305) from the exit section(307) so as to only permit the gas portion (304B) of the insect and gasmixture (304) to flow through the filter element (306) from the entrysection (305) to the exit section (307).

The insect portion (304A) of the insect and gas mixture (304) isretained within the entry section (305) because the pores or openings inthe filter element (306) are smaller than the average insect length(Ni-L) or the average insect width (Ni-W) of the insects (225, Ni)contained within the interior (201) of the feeding chamber (200) andtransferred to the separator (300).

A differential pressure sensor (308) is installed on the separator (300)to measure the pressure drop across the filter element (306) in betweenthe entry section (305) and exit section (307). The differentialpressure sensor (308) is configured to input a signal (309) to thecomputer (COMP). The differential pressure sensor (308) has an entrysection impulse line (310) in fluid communication with the entry section(305) as well as an exit section impulse line (311) in fluidcommunication with the exit section (307).

An insect evacuation fan (312) pulls a vacuum through the separator(300, S1) and in turn pulls a vacuum on the feeding chamber (200). Theinsect evacuation fan (312) is configured to pull a vacuum on thefeeding chamber to remove insects (225) from within the network (220) ofcells 219). Specifically, the insect evacuation fan (312) pulls a vacuumon the network (220) of cells (219) and sucks insects from the inbetween the openings (222) of the first end (221) and the openings (224)of the second end (223) so as to substantially completely evacuateegg-laying insects (225) from the interior (201) of the feeding chamber(200).

When a vacuum is pulled on the feeding chamber the cell networkdifferential pressure sensor (226) sends a signal (227) to the computer(COMP) so as to quantify the quantity of mass of insects (225) presentwithin the network (220) of cells (219) within the feeding chamber (200)interior (201).

The insect evacuation fan (312) is equipped with a fan motor (314) and acontroller (316) that is configured to input and output a signal (318)to the computer (COMP). The insect evacuation fan (312) is connected tothe separator (300) via an insect-depleted gas output (321). Theinsect-depleted gas output (321) is configured to transfer aninsect-depleted gas (320) from the separator (300) to the inlet of theinsect evacuation fan (312). The insect-depleted gas (320) has a reducedamount of insects in it in reference to the insect and gas mixture(304). The insect evacuation fan (312) discharges the insect-depletedgas (320) via an insect-depleted gas exhaust line (322). A portion ofthe insect-depleted gas (320) that passes through the insect-depletedgas exhaust line (322) may be routed back to the separator to backflushthe filter element (306). Thus, the insect-depleted gas exhaust line(322) is in fluid communication with the separator (300) via aninsect-depleted gas recycle line (323) and an exhaust gas recycle input(324).

The separator (300) may be equipped with a valve (325) with a controller(326) that is configured to input a signal (327) to the computer (COMP).The valve (325) is preferably a rotary style valve, but may in someembodiments be that of a ball valve, butterfly valve, knife valve,piston valve, or plug valve.

The separator (300) may also be equipped with a separated insectconveyor (328) to remove separated insects (334) from the separator(300). The separated insect conveyor (328) has a motor (329) and acontroller (330) that is configured to input and output a signal (331)to the computer (COMP). The separated insect conveyor (328) may also beequipped with a mass sensor (332) for weighing the separated insects(334) by sending a signal (333) to the computer (COMP). The separatedinsect conveyor (328) may be any type of conveyor, but preferably is ascrew auger. Other types of conveyors are compression screw conveyors,conveyor belts, a pneumatic conveyor system, a vibrating conveyorsystem, a flexible conveyor system, a vertical conveyor system, a spiralconveyor system, a drag chain conveyor system, or a heavy duty rearconveyor system. Any conceivable type of mechanical handling equipmentmay be used so long as it can move separated insects (334) from onelocation to another. The separated insect conveyor (328) may route theseparated insects (334) to a downstream location such as to a grinder, apathogen removal unit, breeding chamber, a lipid extraction unit, or toa multifunctional composition mixing module.

In embodiments, the insect evacuation fan (312) is configured to removea portion of egg-laying insects from the insect feeding chamber byapplying a vacuum with a velocity pressure range from: between about0.001 inches of water to about 0.005 inches of water; between about0.005 inches of water to about 0.01 inches of water; between about 0.01inches of water to about 0.02 inches of water; between about 0.02 inchesof water to about 0.03 inches of water; between about 0.03 inches ofwater to about 0.04 inches of water; between about 0.04 inches of waterto about 0.05 inches of water; between about 0.05 inches of water toabout 0.06 inches of water; between about 0.06 inches of water to about0.07 inches of water; between about 0.07 inches of water to about 0.08inches of water; between about 0.08 inches of water to about 0.09 inchesof water; between about 0.09 inches of water to about 0.1 inches ofwater; between about 0.1 inches of water to about 0.2 inches of water;between about 0.2 inches of water to about 0.3 inches of water; betweenabout 0.3 inches of water to about 0.4 inches of water; between about0.4 inches of water to about 0.5 inches of water; between about 0.5inches of water to about 0.6 inches of water; between about 0.6 inchesof water to about 0.7 inches of water; between about 0.7 inches of waterto about 0.8 inches of water; between about 0.8 inches of water to about0.9 inches of water; between about 0.9 inches of water to about 1 inchof water; between about 1 inch of water to about 1.25 inches of water;between about 1.25 inches of water to about 1.5 inches of water; betweenabout 1.5 inches of water to about 2 inches of water; between about 2inches of water to about 3 inches of water; between about 3 inches ofwater to about 4 inches of water; between about 4 inches of water toabout 5 inches of water; between about 5 inches of water to about 6inches of water; between about 6 inches of water to about 7 inches ofwater; between about 7 inches of water to about 8 inches of water;between about 8 inches of water to about 9 inches of water; betweenabout 9 inches of water to about 10 inches of water; between about 10inch of water to about 15 inches of water; between about 15 inches ofwater to about 25 inches of water; between about 25 inches of water toabout 50 inches of water; between about 50 inches of water to about 75inches of water; between about 75 inches of water to about 100 inches ofwater; between about 100 inches of water to about 150 inches of water;between about 150 inches of water to about 200 inches of water; betweenabout 200 inches of water to about 250 inches of water; between about250 inches of water to about 300 inches of water; between about 300inches of water to about 350 inches of water; and, between about 350inches of water to about 400 inches of water.

FIG. 3 shows one non-limiting embodiment of an egg transfer system (244)including a conveyor (245) equipped with a first conveyor elevation unit(254) and a second conveyor elevation unit (256) that is configured toextend in a vertical direction from supports (255, 257) from a firstretracted height (H1) to a second elevated height (H2).

The conveyor (245) is configured to make an egg-depleted breedingmaterial (246) available to the interior (201) of the feeding chamber(200). This is achieved by providing a conveyor (245) having anegg-depleted breeding material (246) provided thereon and extending theconveyor (245) in a vertical direction so that the conveyor (245) andegg-depleted breeding material (246) come into contact with the screenfloor (258) of the feeding chamber (200). Egg-laying insects (225) laytheir eggs (259) through the screen floor (258) of the feeding chamber(200) and deposit the eggs (259) into the breeding material (248) thatrests upon the conveyor (245).

In the embodiment of FIG. 3, the egg-laying insects (225) present withinthe interior (201) of the feeding chamber (200) will deposit the eggs(259) into the breeding material (248) and the screen floor (258) willprevent them from eating or digging up the eggs (259). More on thedifferent states of operation is discussed below in FIGS. 5 through 10.

The conveyor (245) receives egg-depleted breeding material (246) via aconveyor input (247). The egg-depleted breeding material (246) is thenmade available to the insects (225) within the feeding chamber (200).This is made possible in the embodiment of FIG. 3 by activating thefirst conveyor elevation unit (254) and second conveyor elevation unit(256) so as to extend the conveyor (245) vertically in a directiontowards the bottom of the feeding chamber (200) from a first retractedheight (H1) to a second elevated height (H2).

After insects (225) have laid their eggs (259) into the breedingmaterial (248), the first conveyor elevation unit (254) and secondconveyor elevation unit (256) are returned from a first retracted height(H1) to a second elevated height (H2) so as to lower the conveyor (245)vertically in a direction away from the bottom of the feeding chamber(200).

As a result of eggs (259) being deposited into the egg-depleted breedingmaterial (246) an egg-laden breeding material (250) is created which isdischarged from the conveyor via a conveyor output (249). The egg-ladenbreeding material (250) has a greater amount of eggs within it inreference to the egg-depleted breeding material (246). The egg-ladenbreeding material (250) is then transferred to a breeding chamber asdescribed below in detail. The conveyor (245) is equipped with aconveyor motor (251) and a controller (252) that is configured to inputand output a signal (253) to the computer (COMP). The first conveyorelevation unit (254) has a first support (255) and the second conveyorelevation unit (256) has a second support (257). The breeding material(248) may be any conceivable material that is suitable for insects todeposit eggs into. In embodiments, the breeding material (248) is soil,mulch, compost, top soil, humus, clay, dirt, sand, minerals, organicmatter, a hydrophobic substance, perlite, vermiculite, a sponge, or acombination thereof.

In embodiments, the breeding material (248) includes a sponge, whereinthe sponge is a synthetic sponge. In embodiments, the breeding material(248) includes a sponge, wherein the sponge is a synthetic sponge. Inembodiments, the synthetic sponge comprises polyester, polyurethane,vegetal cellulose and is a porous material. In embodiments, thesynthetic sponge comprises cellulose derived from wood pulp, sodiumsulphate, hemp fiber. In embodiments, the synthetic sponge comprisesexcellent water retention properties, comprising a flexible, partiallyopen celled foam body made of hydrophobic synthetic material. Inembodiments, the synthetic sponge comprises a body of cellulosic spongematerial. In embodiments, the breeding material (248) includes a sponge,wherein the sponge is a natural or organic sponge.

In embodiments, the breeding material (248) may be comprised of a gel, adamp substrate, vermiculite, leaves, grass clippings, peat moss,agricultural residue, wood chips, green waste, woodchip mulch, barkchips, straw mulch, hay, food waste, animal waste, cardboard, newspaper,carpet, foam, moss, recycled pulp, paper scraps, or feedstock,industrial waste, or any conceivable material that is suitable for aninsect to lay eggs in. In embodiments, the breeding material (248) isused to grow psilocybin mushrooms. In embodiments, the breeding material(248) is used to grow cannabis plants in. In embodiments, the breedingmaterial (248) includes the growing medium used to grow cannabis in. Inembodiments, the breeding material (248) includes cannabis leaves,cannabis stems, cannabis trimmings, cannabis flowers, which may or maynot include cannabinoids.

In embodiments, the breeding material (248) has at a pH selected fromthe group consisting of 4 to 4.5, 4.5 to 5, 5 to 5.5, 5.5 to 6, 6 to6.5, or 6.5 to 7. In embodiments, the breeding material (248) is heatedto remove pathogens from the breeding material (248), wherein thepathogens are comprised of one or more from the group consisting ofacute respiratory syndrome coronavirus, influenza A viruses, H5N1, H7N7,avian influenza, foot and mouth disease, bovine spongiformencephalopathy, Q-fever, cutaneous zoonotic leishmaniasis, Ebola,monkeypox, Rift Valley fever, Crimea Congo hemorrhagic fever,encephalopathy, West Nile fever, paramyxoviruses, viruses, bacteria,fungus, prions, and parasites. In embodiments, the breeding material(248) is heated to kill insects within the breeding material. Inembodiments, the breeding material (248) is heated to kill insect eggsfrom the breeding material. In embodiments, the breeding material (248)is heated to sterilize the breeding material (248). In embodiments, thebreeding material (248) is heated in an oven. In embodiments, thebreeding material (248) is heated to remove volatile compounds orchemicals from the breeding material. In embodiments, the breedingmaterial (248) is heated to remove volatile compounds or chemicals fromthe breeding material by evaporation. In embodiments, the breedingmaterial (248) is directly heated with steam. In embodiments, thebreeding material (248) is indirectly heated with steam. In embodiments,the breeding material (248) is heated in a microwave. In embodiments,pathogens are removed from the breeding material with microwaveradiation. In embodiments, the microwave radiation is in the form ofvariable frequency microwave radiation. In embodiments, the variablefrequency microwave radiation operates at a frequency between about 2GHz to about 8 GHz. In embodiments, the variable frequency microwaveradiation operates at a frequency of about 2.45 GHz.

FIG. 3 also shows that the feeding chamber (200) has a hatched insectsinput (240) that is configured to transfer hatched insects (239) from abreeding chamber to the interior (201) of the feeding chamber (200) viaa breeding chamber insect transfer line (238). In embodiments where theInsect Production Superstructure System (IPSS) may have a plurality ofinsect feeding chambers (FC1, FC2, FC3), the first feeding chamber (FC1)is shown to have an egg-laying insects input (243) for transferringegg-laying insects (242) that were present within the second feedingchamber (FC2) or third feeding chamber (FC3) via a feeding chambertransfer line (241).

In embodiments, the feeding chamber grows insects within it over a timeduration ranging from: between about 1 week to 2 weeks; between about 2weeks to 3 weeks; between about 3 week to 4 weeks; between about 4 weekto 5 weeks; between about 5 week to 6 weeks; between about 6 week to 7weeks; between about 7 week to 8 weeks; between about 8 week to 9 weeks;between about 9 week to 10 weeks; between about 10 week to 11 weeks;between about 11 week to 12 weeks; between about 12 week to 13 weeks;between about 13 week to 14 weeks; or, between about 14 week to 15weeks.

In embodiments, the insects produced within the IPSS have various stagesof growth, including: eggs, larvae, prepupa, pupa, and adult insects. Inembodiments, the various stages of growth include time durations foreach growth stage including: eggs incubated from 1 to 7 days, larvaegrown for a time duration ranging from 1 to 21 days, prepupa grown for atime duration ranging from 7 to 18 days, pupa grown for a time durationranging from 7 to 18 days, and adult insects grown for a time durationranging from 7 to 14 days.

In embodiments, the various stages of growth include time durations foreach growth stage including: eggs incubated from 1 to 7 days, larvaegrown for a time duration ranging from 1 to 21 days, prepupa grown for atime duration ranging from 7 to 18 days, pupa grown for a time durationranging from 7 to 18 days, and adult insects grown for a time durationranging from 1 to 6 weeks.

In embodiments, the interior (201) of the feeding chamber (200) includesa plurality of lights (L1) are configured to be controlled by thecomputer (COMP). In embodiments, the lights (L1) have a controller (CL1)that sends a signal (XL1) to and from the computer (COMP). Inembodiments, the lights (L1, L2) may be compact fluorescent (CFL), lightemitting diode (LED), incandescent lights, fluorescent lights, halogenlights, metal halide lamps, high-intensity discharge (HID) gas dischargelamps, low pressure sodium lamps, sodium lamps, quartz halogen lamps,and combinations thereof.

In embodiments, the lights have a luminous efficacy ratio including oneor more luminous efficacy ratios, measured in lumens per watt, selectedfrom the group consisting of: 30 to 40, 40 to 50, 50 to 60, 60 to 65, 65to 70, 70 to 75, 75 to 80, 80 to 85, 85 to 90, 90 to 95, 95 to 100, 100to 105, 105 to 110, 110 to 115, 115 to 120, 120 to 125, and 125 to 130.In embodiments, the luminous efficacy ratios includes a ratio ofluminous flux to power, measured in lumens per watt. In embodiments, theplurality of lights (L1) operate at a wavelength ranging from 400 nm to700 nm. In embodiment, the plurality of lights (L1) operate at aspectrum including one or more spectrum ranges selected from the groupconsisting of: 390 nanometers (nm) to 400 nm, 400 nm to 410 nm, 410 nmto 420 nm, 420 nm to 430 nm, 430 nm to 440 nm, 440 nm to 450 nm, 450 nmto 460 nm, 460 nm to 470 nm, 470 nm to 480 nm, 480 nm to 490 nm, 490 nmto 500 nm, 500 nm to 510 nm, 510 nm to 520 nm, 520 nm to 530 nm, 530 nmto 540 nm, 540 nm to 550 nm, 550 nm to 560 nm, 560 nm to 570 nm, 570 nmto 580 nm, 580 nm to 590 nm, 590 nm to 600 nm, 600 nm to 610 nm, 610 nmto 620 nm, 620 nm to 630 nm, 630 nm to 640 nm, 640 nm to 650 nm, 650 nmto 660 nm, 660 nm to 670 nm, 670 nm to 680 nm, 680 nm to 690 nm, or 690nm to 700 nm. In embodiments, the adult insects are provided with thesource of light, and adults are grown at a Photosynthetic Photon FluxDensity (in micromole per second and square meter (μmol/m2/s)) rangingfrom 40 to 50, 50 to 60, 60 to 70, 70 to 80, 80 to 90, 90 to 100, 100 to110, 110 to 120, 120 to 130, 130 to 140, 140 to 150, 150 to 160, 160 to170, 170 to 180, 180 to 190, 190 to 200, 200 to 210, 210 to 220, 220 to230, 230 to 240, 240 to 250, 250 to 260, 260 to 270, 270 to 280, 280 to290, or 290 to 300. In embodiments, the adult insects are provided withthe source of light, and adults are grown at a Photosynthetic PhotonFlux Density (in micromole per second and square meter (μmol/m2/s))ranging from 100 to 110 to 130. In embodiments, the PhotosyntheticPhoton Flux Density is based on the number of photons in a certainwaveband incident per unit time (s) on a unit area (m2) divided by theAvogadro constant (6.022×1023 mol-1).

In embodiments, the plurality of lights (L1) operate at a frequencyincluding one or more frequencies selected from the group consisting ofbroad visible spectrum including: 425 terahertz (THz) to 450 THz, 450THz to 475 THz, 475 THz to 500 THz, 500 THz to 525 THz, 525 THz to 550THz, 550 THz to 575 THz, 575 THz to 600 THz, 600 THz to 625 THz, 625 THzto 650 THz, 650 THz to 675 THz, 675 THz to 700 THz, 700 THz to 725 THz,725 THz to 750 THz, 750 THz to 775 THz, or 775 THz to 800 THz.

In embodiments, a plurality of lights (L1) in the interior (201) of thefeeding chamber (200) include a plurality of light emitting diodes(LED). In embodiments, the plurality of light emitting diodes (LED)include blue LEDs (BLED), red LEDS (RLED), and/or green LEDS (GLED). Inembodiments, the plurality of light emitting diodes (LED) in theinterior (201) of the feeding chamber (200) include one or two or morefrom the group consisting of blue LEDs (BLED), red LEDS (RLED), andgreen LEDS (GLED).

In embodiments, the computer (COMP) controls the lights (L1). Inembodiments, the lights (L1) illuminate each the interior (201) of thefeeding chamber (200) with an illumination on-off ratio ranging frombetween 0.5 to 11. The illumination on-off ratio is defined as theduration of time when the lights (L1) are on and illuminate the interior(201) of the feeding chamber (200) in hours divided by the subsequentduration of time when the lights (L1) are off and are not illuminatingthe interior (201) of the feeding chamber (200) in hours before thelights are turned on again.

In embodiments, the lights (L1) are on and illuminate the interior (201)of the feeding chamber (200) for 18 hours and then are turned off for 6hours. 18 divided by 6 is 3. In embodiments, an illumination on-offratio of 3 is contemplated. In embodiments, the lights (L1) are on andilluminate the interior (201) of the feeding chamber (200) for 20 hoursand then are turned off for 4 hours. 20 divided by 4 is 5. Inembodiments, an illumination on-off ratio of 5 is contemplated. Inembodiments, the lights (L1, L2) are on and illuminate the interior(201) of the feeding chamber (200) for 22 hours and then are turned offfor 2 hours. 22 divided by 2 is 11. In embodiments, an illuminationon-off ratio of 11 is contemplated. In embodiments, the lights (L1, L2)are on and illuminate the interior (201) of the feeding chamber (200)for 8 hours and then are turned off for 16 hours. 8 divided by 16 is0.5. In embodiments, an illumination on-off ratio of 0.5 iscontemplated. In embodiments, the lights (L1, L2) are on and illuminatethe interior (201) of the feeding chamber (200) for 12 hours and thenare turned off for 12 hours. 12 divided by 12 is 1. In embodiments, anillumination on-off ratio of 1 is contemplated. In embodiments, the isdesirable to operate the interior (201) of the feeding chamber (200) atan illumination on-off ratio that is greater than 1 and less than 11. Inembodiments, the is desirable to operate the interior (201) of thefeeding chamber (200) at an illumination on-off ratio that is greaterthan 0.5 and equal to or less than 5.

In embodiments, the is illumination on-off ratio for the interior (201)of the feeding chamber (200) includes one or more illumination on-offratios selected from the group consisting of: 0.5 to 0.75, 0.75 to 1, 1to 1.25, 1.25 to 1.5, 1.5 to 1.75, 1.75 to 2, 2 to 2.25, 2.25 to 2.5,2.5 to 2.75, 2.75 to 3, 3 to 3.25, 3.25 to 3.5, 3.5 to 3.75, 3.75 to 4,4 to 4.25, 4.25 to 4.5, 4.5 to 4.75, 4.75 to 5, and 5 to 5.25.

In embodiments, a lights (L1) in the interior (201) of the feedingchamber (200) include a plurality of light emitting diodes (LED). Inembodiments, the plurality of light emitting diodes (LED) include blueLEDs (BLED), red LEDS (RLED), and/or green LEDS (GLED). In embodiments,the plurality of light emitting diodes (LED) in the interior (201) ofthe feeding chamber (200) include one or two or more from the groupconsisting of blue LEDs (BLED), red LEDS (RLED), and green LEDS (GLED).

In embodiments, the blue LEDs (BLED, BLED′) operate at a wavelength thatranges from 490 nanometers (nm) to 455 nm. In embodiments, the red LEDs(RLED, RLED′) operate at a wavelength that ranges from 620 nm to 780 nm.In embodiments, the green LEDs (GLED, GLED′) operate at a wavelengththat ranges from 490 nm to 577 nm. In embodiments, the plurality oflight emitting diodes (LED) are configured to be controlled by acomputer (COMP) to operate at a wavelength ranging from 490 nm to 780nm. In embodiments, the plurality of light emitting diodes (LED) areconfigured to be controlled by a computer (COMP) to operate at awavelength ranging from 400 nm to 700 nm.

In embodiments, the plurality of light emitting diodes (LED) areconfigured to operate in the following manner:

(a) illuminating the interior (201) of the feeding chamber (200) withblue LEDs (BLED, BLED) and red LEDs (RLED, RLED); and

(b) illuminating the interior (201) of the feeding chamber (200) withgreen LEDs (GLED, GLED);

wherein:

the blue LEDs (BLED, BLED′) operate at a wavelength that ranges from 490nanometers to 455 nanometers;

the red LEDs (RLED, RLED′) operate at a wavelength that ranges from 620nanometers to 780 nanometers;

the green LEDs (GLEDGLED′) operate at a wavelength that ranges from 490nanometers to 577 nanometers.

In embodiments, a sensor (OS′) is positioned within the interior of theinterior (201) of the feeding chamber (200), the sensor (OS′) may be anoptical sensor, digital camera, motion sensor, active infrared (AIRs)sensor, passive infrared (PIRs) sensor, microwave motion sensor,continuous wave radar motion sensor (CW), vibration motion sensor, IRsensor, ultrasonic sensor, proximity sensor, and touch sensor, masssensor, laser sensor, or the like.

FIG. 4:

FIG. 4 shows one non-limiting embodiment of a network (220) of cells(219) for growing insects within a feeding chamber (200) of the insectfeeding module (2000) shown in FIG. 3.

FIG. 5:

FIG. 5 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a second mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a second state at a second elevated height (H2) so as topermit insects (225) to lay eggs (259) within a provided breedingmaterial (248).

As discussed above in FIG. 3, FIG. 5 shows the conveyor (245) configuredto make breeding material (248) available to the interior (201) of thefeeding chamber (200). This is achieved by providing a conveyor (245)having a breeding material (248) provided thereon and extending theconveyor (245) in a vertical direction so that the conveyor (245) andegg-depleted breeding material (246) come into contact with the screenfloor (258) of the feeding chamber (200). Egg-laying insects (225) laytheir eggs (259) through the screen floor (258) of the feeding chamber(200) and deposit the eggs (259) into the breeding material (248) thatrests upon the conveyor (245).

In the embodiment of FIG. 5, the egg-laying insects (225) present withinthe interior (201) of the feeding chamber (200) will deposit the eggs(259) into the breeding material (248) and the screen floor (258) willprevent them from eating or digging up the eggs (259). The breedingmaterial (248) is made available to the insects (225) within the feedingchamber (200). This is made possible in the embodiment of FIG. 5 byactivating the first conveyor elevation unit (254) and second conveyorelevation unit (256) so as to extend the conveyor (245) vertically in adirection towards the bottom of the feeding chamber (200) from a firstretracted height (H1) to a second elevated height (H2).

As a result of eggs (259) being deposited into the egg-depleted breedingmaterial (246) an egg-laden breeding material (250) is created which isdischarged from the conveyor via a conveyor output (249). The egg-ladenbreeding material (250) has a greater amount of eggs within it inreference to the egg-depleted breeding material (246).

FIG. 6:

FIG. 6 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) operating in a third mode of operationwherein the egg transfer system (244) of the insect feeding module(2000) is at a first state in a first retracted height (H1) so as todiscontinue insects (225) from laying eggs (259) within the providedbreeding material (248).

As a result of eggs (259) being deposited into the egg-depleted breedingmaterial (246) an egg-laden breeding material (250) is created which isdischarged from the conveyor via a conveyor output (249). The egg-ladenbreeding material (250) has a greater amount of eggs within it inreference to the egg-depleted breeding material (246).

FIG. 7:

FIG. 7 elaborates upon the non-limiting embodiment of FIG. 3 but showsthe insect feeding module (2000) and insect evacuation module (3000)operating in a fourth mode of operation wherein a vibration unit (214)is activated to permit the removal of insects (225) from the network(220) of cells (219) and wherein the insect evacuation module (3000)separates insects from gas while a vacuum is pulled on the insectfeeding module (2000) via an insect evacuation fan (312).

FIG. 8:

FIG. 8 shows a non-limiting embodiment of an insect feeding module(2000) integrated with an insect evacuation module (3000) operating in afirst mode of operation wherein a plurality of slats (341) of an eggtransfer system (244) of the insect feeding module (2000) are in firstclosed state (341A).

Note that in FIG. 8, the enhanced feedstock input (206) is madeavailable to the feeding chamber (206) at a vertical height within theinterior below the network (220) of cells (219).

FIG. 8 discloses another embodiment of the feeding chamber (200) withouta screen floor (258). Instead, a plurality of slats (341) define thebottom of the feeding chamber (200). The plurality of slats (341) areequipped with a slat motor (344) and controller (345) configured torotate the slats (341) upon the input or output of a signal (346) to thecomputer (COMP). The slat motor (344) controller (345) is operativelyequipped to rotate the slats (341) into a plurality of states includinga first closed state (341A) and a second open state (341B). Theembodiments of FIGS. 8 and 9 show the plurality of rotatable slats (341)in the first closed state (341A).

The plurality of slats (341) define the lower section of the interior(201) of the feeding chamber (200) into an upper egg-laying section(342) and a lower egg transfer section (343). The upper egg-layingsection (342) is the region within the interior (201) of the feedingchamber above the plurality of slats (341) and below the network (220)of cells (219) where the insects reside. The lower egg transfer section(343) is the region below the plurality of slats (341) and above the eggtransfer system (244). The embodiment of FIG. 8 depicts the egg transfersystem (244) equipped to output an egg-laden breeding material (339) viaan egg-laden breeding material transfer line (340).

The embodiment of FIG. 8 also depicts the egg transfer system (244)equipped with egg-laden breeding material conveyor (347) with integralmass sensors (351, 353). Insects (225), as well as eggs (259), egg-ladenbreeding material (339) may also be removed via the egg transfer system(244). The egg-laden breeding material conveyor (347) has a motor (348)and a controller (349) that is configured to input and output a signal(350) to the computer (COMP). A first breeding material mass sensor(351) is operatively connected to the egg-laden breeding materialconveyor (347) and is configured to input a signal (352) to the computer(COMP). A second breeding material mass sensor (353) is operativelyconnected to the egg-laden breeding material conveyor (347) and isconfigured to input a signal (354) to the computer (COMP).

In embodiments, plants (107*) are positioned within the interior (201)of the feeding chamber (200). In embodiments, the interior (ENC1) of theenclosure (ENC) of the Farming Superstructure System (FSS) (as disclosedin Volume 2) is positioned within the interior (201) of the feedingchamber (201) of the Insect Production Superstructure System (IPSS) (asdisclosed on Volume I) to permit insects (225) to be co-located withinthe same interior as the plants (107*).

FIG. 9:

FIG. 9 elaborates upon the non-limiting embodiment of FIG. 8 and showsbreeding material (248) resting upon the surface of the plurality ofslats (341) of the egg transfer system (244) so as to permit insects(225) to lay eggs (259) within the breeding material (248).

FIG. 10:

FIG. 10 elaborates upon the non-limiting embodiment FIG. 8 but shows theegg transfer system (244) in a second open state (341A) so as to permitegg-laden breeding material (248) to pass through the plurality of slats(341) while the vibration unit (214) is activated, some insects (225)may pass through the open slats (341) as well.

FIG. 11:

FIG. 11 shows a simplistic diagram illustrating an insect grindingmodule that is configured to grind at least a portion of the insectstransferred from the insect evacuation module (3000). A grinder (1250)is shown to grind the separated insects (334) into a stream of groundseparated insects (1500). The ground separated insects (1500) may besent to the lipid extraction unit (1501) on FIG. 12A, the pathogenremoval unit (1550) on FIG. 13, or the multifunctional compositionmixing module (6000) on FIG. 14A. In embodiments, grinding the insectsreduces the size of the insects. In embodiments, grinding the insects isnot necessary and the insects can be cooked whole to producecooked-whole insects.

In embodiments, the grinder (1250) includes a wet grinder. Inembodiments, the wet grinder is provided with a source of treated water,wherein the treated water is treated with one or more selected from thegroup consisting of a membrane, adsorbent, ion-exchange resin,distillation system, filter, ultraviolent unit, or combinations thereof.In embodiments, the treated water provided to the wet grinder isdescribed in detail elsewhere in this this specification.

FIG. 12A:

FIG. 12A shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000).

FIG. 12A discloses a lipid extraction unit (1501) for extracting insectbased lipids in mass quantities for commercial scale output for use in avariety of areas throughout society. In embodiments, the lipidextraction unit (1501) includes a decanter (1502) having an interior(1505) defined by at least one side wall (1504). A weir (1503) may bepositioned in the decanter (1502). In embodiments, the lipid extractionunit (1501) may be a decanter (1502) in the form of a vertical orhorizontal decanter (1502). Separated insects (334) are provided to thelipid extraction unit (1501) from either the separated insect conveyor(328) via the separator or the ground separated insects (1500) via thegrinder (1250). Separated insects (334) are introduced to the lipidextraction unit (1501) via a separator insect input (1508) andoptionally introduced to the interior (1505) beneath the liquid level ofthe via a diptube (1509).

In embodiments, the lipid extraction unit (1501) is configured toextract lipids by use of a first immiscible liquid (1506) and a secondimmiscible liquid (1507). In embodiments, the first immiscible liquid(1506) has a first density (RHO1) and a first molecular weight (MW1),and the second immiscible liquid (1507) has a second density (RHO2), anda second molecular weight (MW2). In embodiments, first density (RHO1) isgreater than the second density (RHO2). In embodiments, first molecularweight (MW1) is greater than the second molecular weight (MW2).

In embodiments, the first immiscible liquid (1506) is an organiccompound, such as chloroform, with a first density (RHO1) of about 87pounds per cubic foot, and a first molecular weight (MW1) of about 119pound mass per pound mole. In embodiments, the second immiscible liquid(1507) is an alcohol, such as methanol, with a second density (RHO2) ofabout 44 pounds per cubic foot, and a second molecular weight (MW2) ofabout 32 pound mass per pound mole. In embodiments, the first density(RHO1) ranges from between about 70 pounds per cubic foot to about 110pounds per cubic foot. In embodiments, the second density (RHO2) rangesfrom between about 25 pounds per cubic foot to about 69 pounds per cubicfoot. In embodiments, the first molecular weight (MW1) ranges frombetween about 70 pound mass per pound mole to about 150 pound mass perpound mole. In embodiments, the second molecular weight (MW2) rangesfrom between about 18 pound mass per pound mole to about 69 pound massper pound mole.

The weir (1503) separates the decanter (1502) into a first section(1515) and a second section (1516). A first level sensor (1510) ispositioned within the interior (1505) to detect the level of theinterface region (1512) between the first immiscible liquid (1506) andthe second immiscible liquid (1507) within the first section (1515). Thefirst level sensor (1510) is configured to output a signal (1511) to thecomputer (COMP). A second level sensor (1513) is positioned within theinterior (1505) to detect the level of the second immiscible liquid(1507) within the second section (1516). The second level sensor (1513)is configured to output a signal (1514) to the computer (COMP).

In embodiments, a first immiscible liquid and lipid mixture (1518) isformed which is comprised of a lipid portion and a first immiscibleliquid portion. In embodiments, a second immiscible liquid andparticulate mixture (1521) is formed which is comprised of a particulateportion and a second immiscible liquid portion. In embodiments, theparticulate portion is comprised of one or more from the groupconsisting of insect legs, and wings, and protein. In embodiments, thesecond immiscible liquid (1507) floats above first immiscible liquid(1506) in the first section (1515) of the decanter (1502). An interfaceregion (1512) is the region in the first section (1515) of the decanter(1502) in between the upper second immiscible liquid (1507) and thelower first immiscible liquid (1506).

The decanter (1502) has a first immiscible liquid and lipid mixtureoutput (1517) for discharging a first immiscible liquid and lipidmixture (1518) towards a lipid transfer pump (1519). The decanter (1502)also has a second immiscible liquid and particulate mixture output(1520) for discharging a second immiscible liquid and particulatemixture (1521) towards a second immiscible liquid recirculation pump(1522) and particulate filter (1523). The particulate filter (1523) hasa second immiscible liquid input (1524), second immiscible liquid output(1525), and a filtered protein output (1532).

A particulate-depleted second immiscible liquid (1526) is dischargedfrom the second immiscible liquid output (1525) of the particulatefilter (1523) and returned to the decanter (1502) via aparticulate-depleted liquid input (1527). A filtered protein stream(1531) is discharged from the filtered protein output (1532) of theparticulate filter (1523). The decanter (1502) also has an interfacelayer protein take-off point (1528) configured to transfer an interfacelayer protein stream (1529) to an interface layer protein pump (1530).The interface layer protein stream (1529) is comprised of particulatesincluding insect legs, and wings, and protein from the interface region(1512). A temperature sensor (1533) is operatively connected to thelipid extraction unit (1501) and is configured to input a signal (1534)to the computer (COMP).

FIG. 12B:

FIG. 12B shows a simplistic diagram illustrating a lipid extractionmodule that is configured to extract lipids from at least a portion ofthe insects transferred from the insect evacuation module (3000) byusing of no solvent by way of an expeller press.

FIG. 12B shows on non-limiting embodiment wherein lipids may be removedfrom insects without the use of a solvent. Specifically, the lipids maybe extracted from insects by use of a lipid extraction unit (1501) thatincorporates the use of a is a mechanical method for extracting oil. Forexample, one non-limiting embodiment shows the mechanical lipidextraction unit (1501) as an expeller press (1543).

The insects are squeezed through a pressing cage (1549) by the rotatingmotion of a screw press (1546) under high pressure. As the insects arepressed through the pressing cage (1549) by the screw press (1546),friction causes it to heat up. In embodiments, the temperature withinthe expeller press (1543) can increase due to the friction caused byextraction lipids (1541) from the insects. This requires the expellerpress (1543) to require a source of cooling water to cool regulatetemperature and prevent overheating. Ground separated insects (1500)from the separated insect conveyor (328) or insects from any variety offeeding chambers (FC2, FC2, FC3) may be transferred to the lipidextraction unit (1501) by way of a conveyor (1535). The conveyor (1535)transfers lipid laden insects (1537) to the mechanical lipid extractionunit (1501).

The mechanical lipid extraction unit (1501) extracts lipids (1541) fromthe lipid laden insects (1537) to form a stream of lipid depletedinsects (1538). In embodiments, the lipid depleted insects (1538) arecomprised of protein (1542). The conveyor (1535) is equipped with a flowsensor (1536A) that is configured to input/output a signal (1536B) tothe computer (COMP). The conveyor (1535) transfers lipid laden insects(1537) to the feed bin (1544) of the expeller press (1543).

The expeller press (1543) includes a feed bin (1544), motor (1545), andhaving an interior containing a screw press (1546). The screw press(1546) is equipped with a shaft (1547) and flights (1548) and isconfigured to extract lipids from insects by applying pressure on theinsects to squeeze liquid lipids (1541) from the insects. Liquid lipids(1541) extracted from the insects is discharged from the expeller press(1543) through a pressing cage (1549) and a lipid output (1551) and alipid transfer line (1552). A lipid composition sensor (1539) isinstalled on the lipid transfer line (1552) and is configured to inputor output a signal (1540) to the computer (COMP). The expeller press(1543) is equipped with a stand (1555) to elevate off of the ground. Theexpeller press (1543) is equipped with a protein output (1553). Theprotein output (1553) may be an annular nozzle (1554). Lipid depletedinsects (1538) are discharged from the expeller press (1543) via theprotein output (1553). In embodiments, the lipid depleted insects (1538)contain protein (1542). The lipids (1541) may in embodiments be anemulsion. In embodiment, the lipids (1541) emulsion may be an emulsionof oil and water.

The lipid depleted insects (1538) are comprised of a reduced amount oflipids (1541) relative to the lipid laden insects (1537). Lipid depletedinsects (1538) exiting the protein output (1553) are routed to a proteinconveyor (1556). The protein conveyor (1556) is equipped with a pathogensensor (1557) that is configured to input or output a signal (1558) tothe computer (COMP). A protein transfer conduit (1559) is connected tothe protein conveyor (1556) and is configured to remove lipid depletedinsects (1538) containing protein (1542). The mechanical lipidextraction unit (1501) is equipped with a cooling water input (1561) anda cooling water output (1562). A cooling water input temperature sensor(1563) configured to input and output a signal (1564) to the computer(COMP) is installed on the cooling water input (1561). A cooling wateroutput temperature sensor (1566) configured to input and output a signal(1567) to the computer (COMP) is installed on the cooling water output(1562).

In embodiments, the cooling water input temperature sensor (1563) readsa temperature ranging from between about 60 degrees Fahrenheit to about150 degrees Fahrenheit. In embodiments, the cooling water outputtemperature sensor (1566) reads a temperature ranging from between about150.999 degrees Fahrenheit to about 210 degrees Fahrenheit. Inembodiments, the expeller temperature sensor (1568) reads a temperatureranging from between about 60 degrees Fahrenheit to about 210 degreesFahrenheit.

In embodiments, the expeller temperature sensor (1568) reads atemperature, in Fahrenheit, ranging from: −200 to −150, −150 to −100,−100 to −50, −50 to 0, 0 to 10, 10 to 20, 20 to 30, 30 to 40, 40 to 50,50 to 75, 75 to 100, 100 to 125, 125 to 150, 150 to 175, 175 to 200, 200to 225, 225 to 250, 250 to 275, 275 to 300, 300 to 325, 325 to 350, 350to 375, 375 to 400, 400 to 425, 425 to 450, 450 to 475, 475 to 500, 500to 525, 525 to 550, 550 to 575, 575 to 600, 600 to 625, 625 to 650, 650to 675, 675 to 700, 700 to 725, 725 to 750, 750 to 775, or 775 to 800,800 to 900. In embodiments, the lipid extraction unit (1501) is equippedwith an expeller pressure sensor (1571) that is configured to input oroutput a signal to the computer (COMP). In embodiments, the expellerpressure sensor (1571) reads a pressure within the expeller press (1543)ranges from: between about 0.25 PSI to about 49.99 PSI; between about 50PSI to about 99.99 PSI; between about 100 PSI to about 149.99 PSI;between about 150 PSI to about 199.99 PSI; between about 200 PSI toabout 249.99 PSI; between about 250 PSI to about 299.99 PSI; betweenabout 300 PSI to about 349.99 PSI; between about 350 PSI to about 399.99PSI; between about 400 PSI to about 449.99 PSI; between about 450 PSI toabout 499.99 PSI; between about 500 PSI to about 549.99 PSI; betweenabout 550 PSI to about 599.99 PSI; between about 600 PSI to about 649.99PSI; between about 650 PSI to about 699.99 PSI; between about 700 PSI toabout 749.99 PSI; between about 750 PSI to about 799.99 PSI; betweenabout 800 PSI to about 8549.99 PSI; between about 850 PSI to about899.99 PSI; between about 900 PSI to about 949.99 PSI; between about 950PSI to about 999.99 PSI; between about 1,000 PSI to about 1,499.99 PSI;between about 1,500 PSI to about 1,999.99 PSI; between about 2,000 PSIto about 2,499.99 PSI; between about 2,500 PSI to about 2,999.99 PSI;between about 3,000 PSI to about 3,499.99 PSI; between about 3,500 PSIto about 3,999.99 PSI; between about 4,000 PSI to about 4,499.99 PSI;between about 4,500 PSI to about 4,999.99 PSI; between about 5,000 PSIto about 5,499.99 PSI; between about 5,500 PSI to about 5,999.99 PSI;between about 6,000 PSI to about 6,499.99 PSI; between about 6,500 PSIto about 6,999.99 PSI; between about 7,000 PSI to about 7,499.99 PSI;between about 7,500 PSI to about 7,999.99 PSI; between about 8,000 PSIto about 8,499.99 PSI; between about 8,500 PSI to about 8,999.99 PSI;between about 9,000 PSI to about 9,499.99 PSI; between about 9,500 PSIto about 9,999.99 PSI; between about 10,000 PSI to about 15,499.99 PSI;between about 15,500 PSI to about 19,999.99 PSI; between about 20,000PSI to about 25,499.99 PSI; between about 25,500 PSI to about 29,999.99PSI; between about 30,000 PSI to about 35,499.99 PSI; and, between about35,500 PSI to about 40,000 PSI.

It has been my realization that in one non-limiting embodiment the bestmode to operate one scale of an expeller press (1543) is so that theexpeller pressure sensor (1571) reads a pressure of about 250 PSI. Ithas been my realization that in one non-limiting embodiment the bestmode to operate one scale of an expeller press (1543) is so that theexpeller pressure sensor (1571) reads a pressure of about 4,900 PSI. Ithas been my realization that in one non-limiting embodiment the bestmode to operate one scale of an expeller press (1543) is so that theexpeller pressure sensor (1571) reads a pressure of about 19,900 PSI.Nonetheless, all of the above pressures may work as intended to realizelipid extraction from insects.

FIG. 12B shows on non-limiting embodiment wherein cannabinoids arepressed from the cannabis plants. In embodiments, the cannabinoids orcannabis oil (including volatiles, terpenes, wax, and cannabinoids) maybe extracted from cannabis by use a mechanical method for extracting oilas shown in FIG. 12B. In embodiments, the cannabinoids or cannabis oil(including volatiles, terpenes, wax, and cannabinoids) may be extractedfrom cannabis at: a temperature ranging from 50 degrees Fahrenheit to 75degrees Fahrenheit, 75 degrees Fahrenheit to 100 degrees Fahrenheit, 100degrees Fahrenheit to 125 degrees Fahrenheit, 125 degrees Fahrenheit to150 degrees Fahrenheit, 150 degrees Fahrenheit to 175 degreesFahrenheit, 175 degrees Fahrenheit to 200 degrees Fahrenheit, 200degrees Fahrenheit to 225 degrees Fahrenheit, or 250 degrees Fahrenheitto 900 degrees Fahrenheit; and a pressure ranging from between about0.25 PSI to about 49.99 PSI; between about 50 PSI to about 99.99 PSI;between about 100 PSI to about 149.99 PSI; between about 150 PSI toabout 199.99 PSI; between about 200 PSI to about 249.99 PSI; betweenabout 250 PSI to about 299.99 PSI; between about 300 PSI to about 349.99PSI; between about 350 PSI to about 399.99 PSI; between about 400 PSI toabout 449.99 PSI; between about 450 PSI to about 499.99 PSI; betweenabout 500 PSI to about 549.99 PSI; between about 550 PSI to about 599.99PSI; between about 600 PSI to about 649.99 PSI; between about 650 PSI toabout 699.99 PSI; between about 700 PSI to about 749.99 PSI; betweenabout 750 PSI to about 799.99 PSI; between about 800 PSI to about8549.99 PSI; between about 850 PSI to about 899.99 PSI; between about900 PSI to about 949.99 PSI; between about 950 PSI to about 999.99 PSI;between about 1,000 PSI to about 1,499.99 PSI; between about 1,500 PSIto about 1,999.99 PSI; between about 2,000 PSI to about 2,499.99 PSI;between about 2,500 PSI to about 2,999.99 PSI; between about 3,000 PSIto about 3,499.99 PSI; between about 3,500 PSI to about 3,999.99 PSI;between about 4,000 PSI to about 4,499.99 PSI; between about 4,500 PSIto about 4,999.99 PSI; between about 5,000 PSI to about 5,499.99 PSI;between about 5,500 PSI to about 5,999.99 PSI; between about 6,000 PSIto about 6,499.99 PSI; between about 6,500 PSI to about 6,999.99 PSI;between about 7,000 PSI to about 7,499.99 PSI; between about 7,500 PSIto about 7,999.99 PSI; between about 8,000 PSI to about 8,499.99 PSI;between about 8,500 PSI to about 8,999.99 PSI; between about 9,000 PSIto about 9,499.99 PSI; between about 9,500 PSI to about 9,999.99 PSI;between about 10,000 PSI to about 15,499.99 PSI; between about 15,500PSI to about 19,999.99 PSI; between about 20,000 PSI to about 25,499.99PSI; between about 25,500 PSI to about 29,999.99 PSI; between about30,000 PSI to about 35,499.99 PSI; and, between about 35,500 PSI toabout 40,000 PSI. In embodiments, the cannabinoids or cannabis oil(including volatiles, terpenes, wax, and cannabinoids) may be extractedfrom cannabis with hydraulic pressure.

In embodiments, the cannabinoids or cannabis oil (including volatiles,terpenes, wax, and cannabinoids) may be extracted from cannabis withhydraulic pressure using a piston. In embodiments, the piston pressescannabinoids or cannabis oil (including volatiles, terpenes, wax, andcannabinoids) from the cannabis plant. In embodiments, the cannabinoidsor cannabis oil (including volatiles, terpenes, wax, and cannabinoids)pressed from the cannabis plant are filtered. In embodiments, thecannabinoids or cannabis oil (including volatiles, terpenes, wax, andcannabinoids) pressed from the cannabis plant are filtered with afabric. In embodiments, the cannabinoids or cannabis oil (includingvolatiles, terpenes, wax, and cannabinoids) pressed from the cannabisplant as shown in FIG. 12B which shows a simplistic diagram illustratinga cannabinoids or cannabis oil extraction module that is configured toextract cannabinoids or cannabis oil from cannabis by using of nosolvent by way of an expeller press or screw press.

In embodiments, the lipids from the insects may be separated withethanol. In embodiments, the lipids from the insects may be separatedwith carbon dioxide. In embodiments, the lipids from the insects may beseparated with subcritical carbon dioxide. In embodiments, the lipidsfrom the insects may be separated with supercritical critical carbondioxide. In embodiments, the lipids from the insects may be separatedwith carbon dioxide, ethanol, or a solvent as explained in FIGS. 17A′,17A″, 17B′. In embodiments, the lipids from the insects may be separatedwith carbon dioxide as explained in FIGS. 17A′, 17A″, 173. Inembodiments, the lipids from the insects may be separated with ethanolas explained in FIGS. 17A′, 17A″, 17B′.

In embodiments, the cannabinoids or cannabis oil (including volatiles,terpenes, wax, and cannabinoids) pressed from the cannabis plant asshown in FIG. 12B which shows a simplistic diagram illustrating acannabinoids or cannabis oil extraction module that is configured toextract cannabinoids or cannabis oil from cannabis by using of nosolvent by way of an expeller press or screw press.

In embodiments, the protein discharged from the lipid extraction modulemay be introduced to a variety of locations, including: the decanter(1502) of FIG. 12A, or the feedstock tank (1A2) on FIG. 2, or mixed withthe breeding material tank (500) on FIG. 37, or the mixing tank (G15) onFIG. 14G, of the insect liquid mixture tank (H26) on FIG. 14H, or anyother possible area where insects are used.

FIG. 12C:

FIG. 12C shows one non-limiting embodiment of a hydrogenation system(12C) configured to hydrogenate the insect lipids (1518, 1552) toproduce hydrogenation insect lipids (12CC).

In embodiments, the insect lipids (1518, 1552) include palmitic acid,linoleic acid, alpha-linoleic acid, oleic acid, gamma-linoleic acid, orstearic acid: palmitic acid (C15H31COOH) is a saturated fatty acid;linoleic acid (C17H31COOH) is a carboxylic acid, is a polyunsaturatedomega-6 fatty acid; oleic acid (C17H33COOH) monounsaturated omega-9fatty acid; stearic acid (C17H35COOH) is saturated fatty acid. Inembodiments, oleic acid may be hydrogenated into stearic acid. Inembodiments, linoleic acid may be hydrogenated into stearic acid asdepicted in FIG. 12C.

In embodiments, the insect lipids (1518, 1552, 2C58, 2D58) have aviscosity including one or more viscosities selected from the groupconsisting of 5.900 centipoise (cp) to 5.950 cp, 5.950 cp to 6.000 cp,6.000 cp to 6.050 cp, 6.050 cp to 6.100 cp, 6.100 cp to 6.150 cp, 6.150cp to 6.175 cp, 6.175 cp to 6.200 cp, 6.200 cp to 6.225 cp, 6.225 cp to6.250 cp, 6.250 cp to 6.275 cp, 6.275 cp to 6.300 cp, 6.300 cp to 6.325cp, 6.325 cp to 6.350 cp, 6.350 cp to 6.375 cp, 6.375 cp to 6.400 cp,6.400 cp to 6.425 cp, 6.425 cp to 6.450 cp, 6.450 cp to 6.475 cp, 6.475cp to 6.500 cp, 6.500 cp to 6.525 cp, 6.525 cp to 6.550 cp, 6.550 cp to6.575 cp, 6.575 cp to 6.600 cp, 6.600 cp to 6.625 cp, 6.625 cp to 6.650cp, 6.650 cp to 6.675 cp, 6.675 cp to 6.700 cp, 6.700 cp to 6.725 cp,6.725 cp to 6.750 cp, 6.750 cp to 6.775 cp, 6.775 cp to 6.800 cp, 6.800cp to 6.825 cp, 6.825 cp to 6.850 cp, 6.850 cp to 6.875 cp, 6.875 cp to6.900 cp, 6.900 cp to 6.925 cp, 6.925 cp to 6.950 cp, 6.950 cp to 6.975cp, 6.975 cp to 7.000 cp, 7.000 cp to 7.025 cp, 7.025 cp to 7.050 cp,7.050 cp to 7.075 cp, 7.075 cp to 7.100 cp, 7.100 cp to 7.125 cp, 7.125cp to 7.150 cp, 7.150 cp to 7.175 cp, 7.175 cp to 7.200 cp, 7.200 cp to7.225 cp, 7.225 cp to 7.250 cp, 7.250 cp to 7.275 cp, 7.275 cp to 7.300cp, 7.300 cp to 7.325 cp, 7.325 cp to 7.350 cp, 7.350 cp to 7.375 cp,7.375 cp to 7.400 cp, 7.400 cp to 7.425 cp, 7.425 cp to 7.450 cp, 7.450cp to 7.475 cp, 7.475 cp to 7.500 cp, 7.500 cp to 7.525 cp, 7.525 cp to7.550 cp, 7.550 cp to 7.575 cp, 7.575 cp to 7.600 cp, 7.600 cp to 7.625cp, 7.625 cp to 7.650 cp, 7.650 cp to 7.675 cp, 7.675 cp to 7.700 cp,7.700 cp to 7.725 cp, 7.725 cp to 7.750 cp, 7.750 cp to 7.775 cp, 7.775cp to 7.800 cp, 7.800 cp to 7.825 cp, 7.825 cp to 7.850 cp, 7.850 cp to7.875 cp, 7.875 cp to 7.900 cp, 7.900 cp to 7.925 cp, 7.925 cp to 7.950cp, 7.950 cp to 7.975 cp, 7.975 cp to 8.000 cp, 8.000 cp to 8.025 cp,8.025 cp to 8.050 cp, 8.050 cp to 8.075 cp, 8.075 cp to 8.100 cp, 8.100cp to 8.125 cp, 8.125 cp to 8.150 cp, 8.150 cp to 8.175 cp, and 8.175 cpto 8.200 cp.

In embodiments, the insect lipids (1518, 1552, 2C58, 2D58) have amolecular weight including one or more molecular weights selected fromthe group consisting of 280.25 grams per mole (g/mol) to 280.50 g/mol,280.50 g/mol to 280.75 g/mol, 280.75 g/mol to 281.00 g/mol, 281.00 g/molto 281.25 g/mol, 281.25 g/mol to 281.50 g/mol, 281.50 g/mol to 281.75g/mol, 281.75 g/mol to 282.00 g/mol, 282.00 g/mol to 282.25 g/mol,282.25 g/mol to 282.50 g/mol, 282.50 g/mol to 282.75 g/mol, 282.75 g/molto 283.00 g/mol, 283.00 g/mol to 283.25 g/mol, 283.25 g/mol to 283.50g/mol, 283.50 g/mol to 283.75 g/mol, 283.75 g/mol to 284.00 g/mol,284.00 g/mol to 284.25 g/mol, 284.25 g/mol to 284.50 g/mol, 284.50 g/molto 284.75 g/mol, 284.75 g/mol to 285.00 g/mol, 285.00 g/mol to 285.25g/mol, 285.25 g/mol to 285.50 g/mol, 285.50 g/mol to 285.75 g/mol,285.75 g/mol to 286.00 g/mol, 286.00 g/mol to 286.25 g/mol, 286.25 g/molto 286.50 g/mol, 286.50 g/mol to 286.75 g/mol, 286.75 g/mol to 287.00g/mol, 287.00 g/mol to 287.25 g/mol, 287.25 g/mol to 287.50 g/mol,287.50 g/mol to 287.75 g/mol, 287.75 g/mol to 288.00 g/mol, 288.00 g/molto 288.25 g/mol, 288.25 g/mol to 288.50 g/mol, 288.50 g/mol to 288.75g/mol, 288.75 g/mol to 289.00 g/mol, 289.00 g/mol to 289.25 g/mol,289.25 g/mol to 289.50 g/mol, 289.50 g/mol to 289.75 g/mol, 289.75 g/molto 290.00 g/mol, and 290.00 g/mol to 290.25 g/mol.

Insect lipids (1518) from FIG. 12A and/or insect lipids (1552) from FIG.12B may be hydrogenated within a hydrogenation system (12C). The insectlipids (1518, 1522) are introduced to an insect lipid tank (2C1). Theinsect lipid tank (2C1) has an interior (2C2) which contains the insectlipids (1518, 1522). A vacuum (2C3) is configured to be pulled on theinterior (2C2) of the insect lipid tank (2C1). In embodiments, acatalyst (2C99) may be added to the interior (2C2) of the insect lipidtank (2C1) which may then in turn be added to the hydrogenation system(12C). In embodiments, the catalyst (2C99) includes one or morecatalysts selected from the group consisting of a precious metal, morethan one precious metal, gold, silver, platinum, rhodium, palladium,iridium, molybdenum, tungsten, nickel, cobalt, manganese, copper,titanium, silicon, vanadium, copper oxide, zeolite, a sorbent, amolecular sieve, zirconia, alumina, monoclinic or stabilized or dopedzirconia, alkali-earth hexaaluminates, ceria, yittria, lanthanum,magnesium aluminate, promoted alumina, silica, ortitania.

In embodiments, a solvent (2C98) may be added to the interior (2C2) ofthe insect lipid tank (2C1) which may then in turn be added to thehydrogenation system (12C). In embodiments, the solvent (2C98) includesone or more solvent selected from the group consisting of an alcohol, adiglyceride, an ester, ethanol, ethyl acetate, glycerin, glycerol,hexane, hydrocarbon, isopropyl alcohol, methanol, a monoglyceride, and apolyol.

A heat exchanger (2C4) is configured to heat the insect lipids (1518,1522) within the interior (2C2) of the insect lipid tank (2C1). Inembodiments, the insect lipids (1518, 1522) are heated to a temperatureincluding one or more temperature ranges selected from the groupconsisting of: 50 degrees Fahrenheit to 75 degrees Fahrenheit, 75degrees Fahrenheit to 100 degrees Fahrenheit, 100 degrees Fahrenheit to125 degrees Fahrenheit, 125 degrees Fahrenheit to 150 degreesFahrenheit, 150 degrees Fahrenheit to 175 degrees Fahrenheit, 175degrees Fahrenheit to 200 degrees Fahrenheit, 200 degrees Fahrenheit to225 degrees Fahrenheit, 225 degrees Fahrenheit to 250 degreesFahrenheit, 250 degrees Fahrenheit to 275 degrees Fahrenheit, 275degrees Fahrenheit to 300 degrees Fahrenheit, 300 degrees Fahrenheit to325 degrees Fahrenheit, 325 degrees Fahrenheit to 350 degreesFahrenheit, 350 degrees Fahrenheit to 375 degrees Fahrenheit, 375degrees Fahrenheit to 400 degrees Fahrenheit, 400 degrees Fahrenheit to425 degrees Fahrenheit, 425 degrees Fahrenheit to 450 degreesFahrenheit, 450 degrees Fahrenheit to 475 degrees Fahrenheit, 475degrees Fahrenheit to 500 degrees Fahrenheit, 500 degrees Fahrenheit to525 degrees Fahrenheit, 525 degrees Fahrenheit to 550 degreesFahrenheit, 550 degrees Fahrenheit to 575 degrees Fahrenheit, 575degrees Fahrenheit to 600 degrees Fahrenheit, 600 degrees Fahrenheit to625 degrees Fahrenheit, 625 degrees Fahrenheit to 650 degreesFahrenheit, 650 degrees Fahrenheit to 675 degrees Fahrenheit, 675degrees Fahrenheit to 700 degrees Fahrenheit, 700 degrees Fahrenheit to725 degrees Fahrenheit, 725 degrees Fahrenheit to 750 degreesFahrenheit, 750 degrees Fahrenheit to 775 degrees Fahrenheit, 775degrees Fahrenheit to 800 degrees Fahrenheit, 800 degrees Fahrenheit to825 degrees Fahrenheit, 825 degrees Fahrenheit to 850 degreesFahrenheit, 850 degrees Fahrenheit to 875 degrees Fahrenheit, 875degrees Fahrenheit to 900 degrees Fahrenheit, 900 degrees Fahrenheit to925 degrees Fahrenheit, 925 degrees Fahrenheit to 950 degreesFahrenheit, 950 degrees Fahrenheit to 975 degrees Fahrenheit, and 975degrees Fahrenheit to 1000 degrees Fahrenheit.

Heated insect lipids (2C5) are transferred from the insect lipid tank(2C1) to the interior (2C14) of a hydrogenation system (2C13). Thehydrogenation system (2C13) accepts the insect lipids from the insectlipid pump (2C6) via a lipid input (2C12). In embodiments, thehydrogenation system (2C13) includes a heated container configured topromote a hydrogenation reaction of lipids with a source of hydrogengas.

Heated insect lipids (2C5) are transferred from the insect lipid tank(2C1) to an insect lipid pump (2C6). The insect lipid pump (2C6)pressurizes the insect lipids to a pressure including one or morepressure ranges selected from the group consisting of 5 pounds persquare inch (PSI) to 10 PSI, 10 PSI to 20 PSI, 20 PSI to 30 PSI, 30 PSIto 40 PSI, 40 PSI to 50 PSI, 50 PSI to 60 PSI, 60 PSI to 70 PSI, 70 PSIto 80 PSI, 80 PSI to 90 PSI, 90 PSI to 100 PSI, 100 PSI to 125 PSI, 125PSI to 150 PSI, 150 PSI to 175 PSI, 175 PSI to 200 PSI, 200 PSI to 225PSI, 225 PSI to 250 PSI, 250 PSI to 275 PSI, 275 PSI to 300 PSI, 300 PSIto 400 PSI, 400 PSI to 500 PSI, 500 PSI to 600 PSI, 600 PSI to 700 PSI,700 PSI to 800 PSI, 800 PSI to 900 PSI, and 900 PSI to 1,000 PSI.

The insect lipid pump (2C6) passes pressurized heated insect lipidsthrough an insect lipid valve (2C7) prior to introducing the lipids tothe interior (2C14) of the hydrogenation system (2C13). The insect lipidvalve (2C7) is equipped with a controller (2C8) that is configured toinput and/or output a signal (2C9) to and/or from the computer (COMP).

A sensor (2C10) is installed in between the insect lipid pump (2C6) andthe lipid input (2C12) of the hydrogenation system (2C13). The sensor(2C10) is configured to measure the pressure, flow, and/or temperatureof the heated insect lipids and input and/or output a signal (2C11) tothe computer (COMP). In embodiments, the flow of the insect lipidsthrough the sensor (2C10) includes one or more from the group consistingof: 0.5 gallons per minute (GPM) to 1 GPM, 1 GPM to 1.5 GPM, 1.5 GPM to2 GPM, 2 GPM to 2.5 GPM, 2.5 GPM to 3 GPM, 3 GPM to 3.5 GPM, 3.5 GPM to4 GPM, 4 GPM to 4.5 GPM, 4.5 GPM to 5 GPM, 5 GPM to 5.5 GPM, 5.5 GPM to6 GPM, 6 GPM to 6.5 GPM, 6.5 GPM to 7 GPM, 7 GPM to 7.5 GPM, 7.5 GPM to8 GPM, 8 GPM to 8.5 GPM, 8.5 GPM to 9 GPM, 9 GPM to 9.5 GPM, 9.5 GPM to10 GPM, and 10 GPM to 10.5 GPM.

In embodiments, the hydrogenation system (2C13) includes a top (2CT) anda bottom (2CB) that are spaced apart along a vertical axis (2CV). Thehydrogenation system (2C13) has a vertical axis (2CV) and a horizontalaxis (2CH). In embodiments, the range of height of the hydrogenationsystem (2C13) is selected from one or more from the group consisting of1 foot tall to 2 feet tall, 2 feet tall to 3 feet tall, 4 feet tall to 5feet tall, 6 feet tall to 8 feet tall, 8 feet tall to 10 feet tall, 10feet tall to 12 feet tall, 12 feet tall to 14 feet tall, 14 feet tall to16 feet tall, 16 feet tall to 18 feet tall, 18 feet tall to 20 feettall, 20 feet tall to 22 feet tall, 22 feet tall to 24 feet tall, 24feet tall to 26 feet tall, 26 feet tall to 28 feet tall, 28 feet tall to30 feet tall, 30 feet tall to 32 feet tall, 32 feet tall to 34 feettall, 34 feet tall to 36 feet tall, 36 feet tall to 38 feet tall, 38feet tall to 40 feet tall, and 40 feet tall to 50 feet tall. Inembodiments, the hydrogenation system (2C13) is comprised of a materialthat is selected from one or more from the group consisting of glass,borosilicated glass, carbon steel, graphite, Hastelloy alloy, nickel,stainless steel, tantalum, and titanium.

In embodiments, the hydrogenation system (2C13) is equipped with a motor(2C15) that is configured to turn a shaft (2C16). In embodiments, themotor (2C15) rotates the shaft (2C16) at a revolutions per minute (rpm)including one or more rpm ranges selected from the group consisting of:25 rpm to 50 rpm, 50 rpm to 75 rpm, 75 rpm to 100 rpm, 100 rpm to 125rpm, 125 rpm to 150 rpm, 150 rpm to 175 rpm, 175 rpm to 200 rpm, 200 rpmto 225 rpm, 225 rpm to 250 rpm, 250 rpm to 275 rpm, 275 rpm to 300 rpm,300 rpm to 325 rpm, 325 rpm to 350 rpm, 350 rpm to 375 rpm, 375 rpm to400 rpm, 400 rpm to 425 rpm, 425 rpm to 450 rpm, 450 rpm to 475 rpm, 475rpm to 500 rpm, 500 rpm to 525 rpm, 525 rpm to 550 rpm, 550 rpm to 575rpm, 575 rpm to 600 rpm, 600 rpm to 625 rpm, 625 rpm to 650 rpm, 650 rpmto 675 rpm, 675 rpm to 700 rpm, 700 rpm to 725 rpm, 725 rpm to 750 rpm,750 rpm to 775 rpm, 775 rpm to 800 rpm, 800 rpm to 825 rpm, 825 rpm to850 rpm, 850 rpm to 875 rpm, 875 rpm to 900 rpm, 900 rpm to 925 rpm, 925rpm to 950 rpm, 950 rpm to 975 rpm, 975 rpm to 1000 rpm, 1000 rpm to1100 rpm, 1100 rpm to 1200 rpm, 1200 rpm to 1300 rpm, 1300 rpm to 1400rpm, 1400 rpm to 1500 rpm, 1500 rpm to 2000 rpm. An impeller (2C17) or aplurality of impellers (2C17) are connected to the shaft. Theimpeller(s) (2C17) are configured to agitate the insect lipid mixturewithin the interior (2C14) of the hydrogenation system (2C13) andpromote mixing between the insect lipids and a source of hydrogen gas.In embodiments, the shaft (2C16) is positioned on an angle disposed intothe interior (2C14) hydrogenation system (2C13) below the liquid level(2C28) on an angle that ranges from: 3 degrees to 5 degrees, 5 degreesto 8 degrees, 8 degrees to 11 degrees, 11 degrees to 14 degrees, and 14degrees to 20 degrees.

A source of steam (LZC) is provided to the hydrogenation system (2C13).In embodiments, the source of steam (LZC) is mixed with the insectlipids and hydrogen gas within the interior (2C14) of the hydrogenationsystem (2C13). In embodiments, the source of steam (LZC) is providedfrom the twelfth steam valve (LZB) as shown on FIG. 14L. The source ofsteam (LZC) is provided from a steam distribution header (LCJ) on thepower production system as depicted below on FIG. 14L.

In embodiments, a steam valve (2C20) is configured to transfer thesource of steam (LZC) to a steam input (2C23) of a heating jacket(2C24). The heating jacket (2C24) is in indirect thermal contact withthe interior (2C14) of the hydrogenation system (2C13). Heat from thesteam (LZC) is transferred through a heat transfer surface of theheating jacket (2C24) to the insect lipids and hydrogen gas within theinterior (2C14) of the hydrogenation system (2C13). In embodiments, thesteam valve (2C20) is equipped with a controller (2C21) that isconfigured to input and/or output a signal (2C22) to the computer(COMP). The heating jacket (2C24) has a heat transfer medium output(2C25) for discharging the steam condensate (2C26) from the heatingjacket (2C24).

In embodiments, the interior (2C14) of the hydrogenation system (2C13)is equipped with a baffle (2C27) or a plurality of baffles (2C27). Inembodiments, the baffles(s) (2C27) include flow-directing or obstructingvanes or panels that are connected to the interior (2C14) of thehydrogenation system (2C13). In embodiments, the baffles(s) (2C27)permit axial circulation within the hydrogenation system (2C13). Inembodiments, the hydrogenation system (2C13) includes a cylindricaltank. In embodiments, the liquid level (2C28) within the interior (2C14)of the hydrogenation system (2C13) is maintained at a pre-determinedheight.

A source of hydrogen (2C29) is made available to the interior (2C14) ofthe hydrogenation system (2C13) via a hydrogen input (2C36). Inembodiments, a hydrogen distributor (2C37) is configured tosubstantially uniformly distribute the source of hydrogen (2C29) to theinterior (2C14) of the hydrogenation system (2C13). In embodiments, thehydrogen distributor (2C37) is configured to substantially uniformlydistribute the source of hydrogen (2C29) to the interior (2C14) of thehydrogenation system (2C13) via a plurality of restrictions whilebubbling up through the heated insect lipids.

In embodiments, the pressure drop of the source of hydrogen (2C29)across the hydrogen distributor (2C37) (or the plurality ofrestrictions) ranges from one or more pressure drop ranges selected fromthe group consisting of: 5 pounds per square inch (PSI) to 10 PSI, 10PSI to 20 PSI, 20 PSI to 30 PSI, 30 PSI to 40 PSI, 40 PSI to 50 PSI, 50PSI to 60 PSI, 60 PSI to 70 PSI, 70 PSI to 80 PSI, 80 PSI to 90 PSI, 90PSI to 100 PSI, 100 PSI to 125 PSI, 125 PSI to 150 PSI, 150 PSI to 175PSI, 175 PSI to 200 PSI, 200 PSI to 225 PSI, 225 PSI to 250 PSI, 250 PSIto 275 PSI, 275 PSI to 300 PSI, 300 PSI to 400 PSI, 400 PSI to 500 PSI,500 PSI to 600 PSI, 600 PSI to 700 PSI, 700 PSI to 800 PSI, 800 PSI to900 PSI, and 900 PSI to 1,000 PSI.

In embodiments, a hydrogen valve (2C30) is equipped to regulate the flowof the source of hydrogen (2C29) that is introduced to the interior(2C14) of the hydrogenation system (2C13). In embodiments, the hydrogenvalve (2C30) is equipped with a controller (2C31) that is configured toinput and/or output a signal (2C32) to and/or from the computer (COMP).In embodiments, the hydrogen valve (2C30) percent open during normaloperation ranges from 10% open to 25% open, 25% open to 35% open, 35%open to 45% open, 45% open to 55% open, 55% open to 65% open, 65% opento 75% open, 75% open to 80% open. In embodiments, the pressure dropacross the hydrogen valve (2C30) ranges from between 5 PSI to 10 PSI, 15PSI to 25 PSI, 25 PSI to 35 PSI, 35 PSI to 45 PSI, 45 PSI to 55 PSI, 55PSI to 65 PSI, 65 PSI to 75 PSI, 75 PSI to 85 PSI.

In embodiments, a sensor (2C33) is configured to analyze the hydrogen(2C29) before it is transferred to the interior (2C14) of thehydrogenation system (2C13). In embodiments, the sensor (2C33) includesa temperature sensor, a pressure sensor, a gas quality sensor, amoisture sensor, or a flow sensor. In embodiments, the sensor (2C33) isconfigured to input a signal (2C34) to the computer (COMP). Inembodiments, the source of hydrogen (2C29) passes through a one-wayvalve (2C35) before it is transferred to the interior (2C14) of thehydrogenation system (2C13). In embodiments, the one-way valve (2C35)prevents flow of the insect lipid mixture within the interior (2C14) ofthe hydrogenation system (2C13) to flow backwards and clog up thehydrogen valve (2C30).

A source of gas (2C38) is made available to the interior (2C14) of thehydrogenation system (2C13) via a gas input (2C45). In embodiments, agas valve (2C39) is equipped to regulate the flow of the source of gas(2C38) that is introduced to the interior (2C14) of the hydrogenationsystem (2C13). In embodiments, the gas valve (2C39) is equipped with acontroller (2C40) that is configured to input and/or output a signal(2C41) to and/or from the computer (COMP). In embodiments, the gas valve(2C39) percent open during normal operation ranges from 10% open to 25%open, 25% open to 35% open, 35% open to 45% open, 45% open to 55% open,55% open to 65% open, 65% open to 75% open, 75% open to 80% open. Inembodiments, the pressure drop across the gas valve (2C39) ranges frombetween 5 PSI to 10 PSI, 15 PSI to 25 PSI, 25 PSI to 35 PSI, 35 PSI to45 PSI, 45 PSI to 55 PSI, 55 PSI to 65 PSI, 65 PSI to 75 PSI, 75 PSI to85 PSI.

In embodiments, a sensor (2C43) is configured to analyze the gas (2C38)before it is transferred to the interior (2C14) of the hydrogenationsystem (2C13). In embodiments, the sensor (2C43) includes a temperaturesensor, a pressure sensor, a gas quality sensor, a moisture sensor, or aflow sensor. In embodiments, the sensor (2C43) is configured to input asignal (2C42) to the computer (COMP). In embodiments, the gas input(2C45) introduces the gas (2C38) to the interior (2C14) hydrogenationsystem (2C13) above the liquid level (2C28). In embodiments, the gas(2C38) includes one or more inert gases selected from the groupconsisting of argon, nitrogen, carbon dioxide, air, oxygen, and helium.In embodiments, the gas (2C38) forms a protective atmosphere (preventoxidation and/or degradation of the hydrogenated lipids, improvedproduct quality, clean good manufacturing practices as required bypharmaceutical industry, for cleaning in place, etc.) whilehydrogenating the insect lipids.

In embodiments, the source of gas (2C38) passes through a one-way valve(2C44) before it is transferred to the gas input (2C45) of thehydrogenation system (2C13). In embodiments, the one-way valve (2C35)prevents flow of the insect lipid mixture within the interior (2C14) ofthe hydrogenation system (2C13) to flow backwards and clog up the gasvalve (2C39).

In embodiments, a vacuum system (2C46) is configured to pull a vacuum onthe interior (2C14) of the hydrogenation system (2C13) via agas-vapor-mixture output (2C49). A gas-vapor-mixture (2C48) is evacuatedfrom the interior (2C14) of the hydrogenation system (2C13) via thegas-vapor-mixture output (2C49). In embodiments, the gas-vapor-mixture(2C48) passes through a condenser (2C47) before being introduced to thevacuum system (2C46). In embodiments, at least a portion of the vaporwithin the gas-vapor-mixture (2C48) is condensed within the condenser(2C47). A gas (2C50) is evacuated from the vacuum system (2C46). Inembodiments, the vacuum system (2C46) includes a device that removes gasmolecules from interior (2C14) of the hydrogenation system (2C13) inorder to leave behind a partial vacuum. In embodiments, the vacuumsystem (2C46) includes a rotary vane pump, diaphragm pump, liquid ringvacuum pump, piston pump, scroll pump, screw pump, Wankel pump, externalvane pump, roots blower, booster pump, Toepler pump, lobe pump, venturi,eductor, or an ejector.

In embodiments, hydrogenated insect lipids (2C51) are discharged fromthe interior (2C14) of the hydrogenation system (2C13) via a lipidoutput (2C52). A hydrogenated insect lipid pump (2C53) is configured topump hydrogenated insect lipids (2C51) from the interior (2C14) of thehydrogenation system (2C13) via the lipid output (2C52). Thehydrogenated insect lipid pump (2C53) pumps and pressurizes thehydrogenated insect lipids (2C51) to formpressurized-hydrogenated-insect-lipids (2C54) which is then transferredto the interior (2C56) of a hydrogenated insect lipid tank (2C55). Thehydrogenated insect lipids (2C51) are introduced to the interior (2C56)of a hydrogenated insect lipid tank (2C55). The hydrogenated insectlipid tank (2C55) has an interior (2C56) which contains the hydrogenatedinsect lipids (2C51). The vacuum system (2C46) is configured to pull avacuum on the interior (2C56) of the hydrogenated insect lipid tank(2C55).

A heat exchanger (2C57) is configured to heat the hydrogenated insectlipids (2C51) within the interior (2C56) of a hydrogenated insect lipidtank (2C55). In embodiments, the hydrogenated insect lipids (2C51) areheated to a temperature including one or more temperature rangesselected from the group consisting of: 50 degrees Fahrenheit to 75degrees Fahrenheit, 75 degrees Fahrenheit to 100 degrees Fahrenheit, 100degrees Fahrenheit to 125 degrees Fahrenheit, 125 degrees Fahrenheit to150 degrees Fahrenheit, 150 degrees Fahrenheit to 175 degreesFahrenheit, 175 degrees Fahrenheit to 200 degrees Fahrenheit, 200degrees Fahrenheit to 225 degrees Fahrenheit, 225 degrees Fahrenheit to250 degrees Fahrenheit, 250 degrees Fahrenheit to 275 degreesFahrenheit, 275 degrees Fahrenheit to 300 degrees Fahrenheit, 300degrees Fahrenheit to 325 degrees Fahrenheit, 325 degrees Fahrenheit to350 degrees Fahrenheit, 350 degrees Fahrenheit to 375 degreesFahrenheit, 375 degrees Fahrenheit to 400 degrees Fahrenheit, 400degrees Fahrenheit to 425 degrees Fahrenheit, 425 degrees Fahrenheit to450 degrees Fahrenheit, 450 degrees Fahrenheit to 475 degreesFahrenheit, 475 degrees Fahrenheit to 500 degrees Fahrenheit.

Heated hydrogenated insect lipids (2C58) are transferred from theinterior (2C56) of a hydrogenated insect lipid tank (2C55) to anotherhydrogenated insect lipid pump (2C59) which pumps and pressurizes theheated hydrogenated insect lipids (2C58) to formpressurized-hydrogenated-insect-lipids which is then transferred to theinterior (2D02) of an esterification system (2D01) as shown on FIG. 12D.

The hydrogenated insect lipid pump (2C59) passespressurized-hydrogenated-insect-lipids through a hydrogenated insectlipid valve (2C60) prior to introducing the lipids to the interior(2D02) of an esterification system (2D01) as shown on FIG. 12D. Thehydrogenated insect lipid valve (2C60) is equipped with a controllerthat is configured to input and/or output a signal to and/or from thecomputer.

FIG. 12C shows one non-limiting embodiment of a hydrogenation system(12C) configured to hydrogenate the cannabis oil to producehydrogenation cannabis oil.

FIG. 12D:

FIG. 12D shows one non-limiting embodiment of an esterification system(12D) configured to produce esterified insect lipids.

In embodiments, an ester may be produced by esterification of an esterof an alcohols and/or a polyol (ethylene glycol and glycerol) withinsect lipids (1518, 1552) (as shown in FIGS. 12A and 12B) and/orhydrogenated insect lipids (2C58), as described in FIG. 12C. Inembodiments, the insect lipids (1518, 1552) (as shown in FIGS. 12A and12B) and/or hydrogenated insect lipids (2C58), as described in FIG. 12Cdescribed herein may undergo direct esterification, for example withglycerol. In embodiments, stearic acid is reacted with glycerol toproduce glyceryl stearate. In embodiments, stearic acid is reacted withglycerol to produce glyceryl stearate in the presence of a catalyst.

Insect lipids (1518, 1552) and/or hydrogenated insect lipids (2C58) maybe hydrogenated within the interior (2D13) of an esterification system(2D13). The insect lipids (1518, 1522, 2C58) are introduced the interior(2D13) of an esterification system (2D13). The esterification system(2D13) has an interior (2D14) which contains the insect lipids (1518,1522, 2C58), an acid (2D90), a catalyst (2D91), and optionally a solventas described in FIG. 12C.

In embodiment, the acid (2D90) includes one or more acids selected fromthe group consisting of abscic acid, acetic acid, ascorbic acid, benzoicacid, citric acid, formic acid, fumaric acid, hydrochloric acid, lacticacid, malic acid, nitric acid, organic acids, phosphoric acid, potassiumhydroxide, propionic acid, salicylic acid, sulfamic acid, sulfuric acid,tartaric acid, and tosylic acid.

A vacuum (2D3) is configured to be pulled on the interior (2D13) of anesterification system (2D13). In embodiments, a catalyst (2D91) may beadded to the interior (2D13) of an esterification system (2D13). Inembodiments, the catalyst (2C91) includes one or more catalysts selectedfrom the group consisting of a precious metal, more than one preciousmetal, gold, silver, platinum, rhodium, palladium, iridium, molybdenum,tungsten, nickel, cobalt, manganese, copper, titanium, silicon,vanadium, copper oxide, zeolite, a sorbent, a molecular sieve, zirconia,alumina, monoclinic or stabilized or doped zirconia, alkali-earthhexaaluminates, ceria, yittria, lanthanum, magnesium aluminate, promotedalumina, silica, ortitania.

In embodiments, a solvent (2D92) may be added to the interior (2D13) ofan esterification system (2D13). In embodiments, the solvent (2D92)includes one or more solvent selected from the group consisting of analcohol, a diglyceride, an ester, ethanol, ethyl acetate, glycerin,glycerol, hexane, hydrocarbon, isopropyl alcohol, methanol, amonoglyceride, and a polyol.

Insect lipids (1518, 1522, 2C58) are transferred to the interior (2D13)of an esterification system (2D13). The esterification system (2D13)accepts the insect lipids from: lipid extraction unit (1501) disclose onFIGS. 12A-B, and/or the hydrogenation system (2C13) on FIG. 12D. Inembodiments, the esterification system (2D13) includes a heatedcontainer configured to promote an esterification reaction between thesolvent (2D92) and the lipids (1518, 1522, 2C58) in the presence of asource of inert gas (2D38).

In embodiments, the esterification system (2D13) includes a top (2DT)and a bottom (2DB) that are spaced apart along a vertical axis (2DV).The esterification system (2D13) has a vertical axis (2DV) and ahorizontal axis (2DH). In embodiments, the range of height of theesterification system (2D13) is selected from one or more from the groupconsisting of 1 foot tall to 2 feet tall, 2 feet tall to 3 feet tall, 4feet tall to 5 feet tall, 6 feet tall to 8 feet tall, 8 feet tall to 10feet tall, 10 feet tall to 12 feet tall, 12 feet tall to 14 feet tall,14 feet tall to 16 feet tall, 16 feet tall to 18 feet tall, 18 feet tallto 20 feet tall, 20 feet tall to 22 feet tall, 22 feet tall to 24 feettall, 24 feet tall to 26 feet tall, 26 feet tall to 28 feet tall, 28feet tall to 30 feet tall, 30 feet tall to 32 feet tall, 32 feet tall to34 feet tall, 34 feet tall to 36 feet tall, 36 feet tall to 38 feettall, 38 feet tall to 40 feet tall, and 40 feet tall to 50 feet tall. Inembodiments, the esterification system (2D13) is comprised of a materialthat is selected from one or more from the group consisting of glass,borosilicated glass, carbon steel, graphite, Hastelloy alloy, nickel,stainless steel, tantalum, and titanium.

In embodiments, the esterification system (2D13) is equipped with amotor (2D15) that is configured to turn a shaft (2D16). In embodiments,the motor (2D15) rotates the shaft (2D16) at a revolutions per minute(rpm) including one or more rpm ranges selected from the groupconsisting of: 25 rpm to 50 rpm, 50 rpm to 75 rpm, 75 rpm to 100 rpm,100 rpm to 125 rpm, 125 rpm to 150 rpm, 150 rpm to 175 rpm, 175 rpm to200 rpm, 200 rpm to 225 rpm, 225 rpm to 250 rpm, 250 rpm to 275 rpm, 275rpm to 300 rpm, 300 rpm to 325 rpm, 325 rpm to 350 rpm, 350 rpm to 375rpm, 375 rpm to 400 rpm, 400 rpm to 425 rpm, 425 rpm to 450 rpm, 450 rpmto 475 rpm, 475 rpm to 500 rpm, 500 rpm to 525 rpm, 525 rpm to 550 rpm,550 rpm to 575 rpm, 575 rpm to 600 rpm, 600 rpm to 625 rpm, 625 rpm to650 rpm, 650 rpm to 675 rpm, 675 rpm to 700 rpm, 700 rpm to 725 rpm, 725rpm to 750 rpm, 750 rpm to 775 rpm, 775 rpm to 800 rpm, 800 rpm to 825rpm, 825 rpm to 850 rpm, 850 rpm to 875 rpm, 875 rpm to 900 rpm, 900 rpmto 925 rpm, 925 rpm to 950 rpm, 950 rpm to 975 rpm, 975 rpm to 1000 rpm,1000 rpm to 1100 rpm, 1100 rpm to 1200 rpm, 1200 rpm to 1300 rpm, 1300rpm to 1400 rpm, 1400 rpm to 1500 rpm, 1500 rpm to 2000 rpm.

An impeller (2D17) or a plurality of impellers (2D17) are connected tothe shaft. The impeller(s) (2D17) are configured to agitate a liquidmixture within the interior (2D14) of the esterification system (2D13)and promote mixing between the insect lipids and a source of solvent. Inembodiments, the shaft (2D16) is positioned on an angle disposed intothe interior (2D14) hydrogenation system (2D13) below the liquid level(2D28) on an angle that ranges from: 3 degrees to 5 degrees, 5 degreesto 8 degrees, 8 degrees to 11 degrees, 11 degrees to 14 degrees, and 14degrees to 20 degrees.

A source of steam (2D95) is provided to the esterification system(2D13). In embodiments, the source of steam (2D95) is mixed with theliquid within the interior (2D14) of the esterification system (2D13).In embodiments, the source of steam is provided from a steam valve onFIG. 14L which is described in detail on FIG. 12C. The source of steam(2D95) is provided from a steam distribution header on the powerproduction system as depicted below on FIG. 14L.

In embodiments, a steam valve (2D96) is configured to transfer thesource of steam (2D95) to a steam input (2D23) of a heating jacket(2D24). The heating jacket (2D24) is in indirect thermal contact withthe interior (2D14) of the esterification system (2D13). Heat from thesteam (2D95) is transferred through a heat transfer surface of theheating jacket (2D24) to the liquid mixture within the interior (2 d 14)of the esterification system (2D13). In embodiments, the steam valve(2D96) is equipped with a controller (2D97) that is configured to inputand/or output a signal (2D98) to the computer (COMP). The heating jacket(2D24) has a heat transfer medium output (2D25) for discharging thesteam condensate (2D26) from the heating jacket (2D24).

In embodiments, the interior (2D14) of the esterification system (2D13)is equipped with a baffle (2D27) or a plurality of baffles (2D27). Inembodiments, the baffles(s) (2D27) include flow-directing or obstructingvanes or panels that are connected to the interior (2D14) of theesterification system (2D13). In embodiments, the baffles(s) (2D27)permit axial circulation within the esterification system (2D13). Inembodiments, the esterification system (2D13) includes a cylindricaltank. In embodiments, a liquid level (2D28) within the interior (2D14)of the esterification system (2D13) is maintained at a pre-determinedheight.

A source of catalyst (2D91) is made available to the interior (2D14) ofthe esterification system (2D13) via a catalyst input (2D36). Inembodiments, the catalyst (2C99) includes one or more catalysts selectedfrom the group consisting of a precious metal, more than one preciousmetal, gold, silver, platinum, rhodium, palladium, iridium, molybdenum,tungsten, nickel, cobalt, manganese, copper, titanium, silicon,vanadium, copper oxide, zeolite, a sorbent, a molecular sieve, zirconia,alumina, monoclinic or stabilized or doped zirconia, alkali-earthhexaaluminates, ceria, yittria, lanthanum, magnesium aluminate, promotedalumina, silica, ortitania.

A source of gas (2D38) is made available to the interior (2D14) of theesterification system (2D13) via a gas input (2D45). In embodiments, agas valve (2D39) is equipped to regulate the flow of the source of gas(2D38) that is introduced to the interior (2D14) of the esterificationsystem (2D13). In embodiments, the gas valve (2D39) is equipped with acontroller (2D40) that is configured to input and/or output a signal(2D41) to and/or from the computer (COMP). In embodiments, the gas valve(2D39) percent open during normal operation ranges from 10% open to 25%open, 25% open to 35% open, 35% open to 45% open, 45% open to 55% open,55% open to 65% open, 65% open to 75% open, 75% open to 80% open. Inembodiments, the pressure drop across the gas valve (2C39) ranges frombetween 5 PSI to 10 PSI, 15 PSI to 25 PSI, 25 PSI to 35 PSI, 35 PSI to45 PSI, 45 PSI to 55 PSI, 55 PSI to 65 PSI, 65 PSI to 75 PSI, 75 PSI to85 PSI.

In embodiments, a sensor (2D43) is configured to analyze the gas (2D38)before it is transferred to the interior (2D14) of the esterificationsystem (2D13). In embodiments, the sensor (2D43) includes a temperaturesensor, a pressure sensor, a gas quality sensor, a moisture sensor, or aflow sensor. In embodiments, the sensor (2D43) is configured to input asignal (2D42) to the computer (COMP). In embodiments, the gas input(2D45) introduces the gas (2D38) to the interior (2D14) of theesterification system (2D13) above the liquid level (2C28). Inembodiments, the gas (2D38) includes one or more inert gases selectedfrom the group consisting of argon, nitrogen, carbon dioxide, air,oxygen, and helium. In embodiments, the gas (2D38) forms a protectiveatmosphere (prevent oxidation and/or degradation of the hydrogenatedlipids, esterified lipids, improved product quality, clean goodmanufacturing practices as required by pharmaceutical industry, forcleaning in place, etc.) while esterifying the insect lipids.

In embodiments, the source of gas (2D38) passes through a one-way valve(2D44) before it is transferred to the gas input (2D45) of theesterification system (2D13). In embodiments, the one-way valve (2D35)prevents flow of the liquid mixture within the interior (2D14) of theesterification system (2D13) to flow backwards and clog up the gas valve(2D39).

In embodiments, a vacuum system (2D46) is configured to pull a vacuum onthe interior (2D14) of the esterification system (2D13) via agas-vapor-mixture output (2D49). A gas-vapor-mixture (2D48) is evacuatedfrom the interior (2D14) of the esterification system (2D13) via thegas-vapor-mixture output (2D49). In embodiments, the gas-vapor-mixture(2D48) passes through a condenser (2D47) before being introduced to thevacuum system (2D46). In embodiments, at least a portion of the vaporwithin the gas-vapor-mixture (2D48) is condensed within the condenser(2D47). A gas (2D50) is evacuated from the vacuum system (2D6). Inembodiments, the vacuum system (2D46) includes a device that removes gasmolecules from interior (2D14) of the esterification system (2D13) inorder to leave behind a partial vacuum. In embodiments, the vacuumsystem (2D46) includes a rotary vane pump, diaphragm pump, liquid ringvacuum pump, piston pump, scroll pump, screw pump, Wankel pump, externalvane pump, roots blower, booster pump, Toepler pump, lobe pump, venturi,eductor, or an ejector.

In embodiments, esterified lipids (2D51) are discharged from theinterior (2D14) of the esterification system (2D13) via an output(2D52). An esterified lipid pump (2D53) is configured to pump esterifiedlipids (2D51) from the interior (2D14) of the esterification system(2D13) via the output (2D52). The esterified lipid pump (2D53) pumps andpressurizes the esterified lipids (2D51) to formpressurized-esterified-lipids (2D58) which are then transferred to afilter (2D60) to produce filtered lipids (2D61). In embodiments, aportion of the esterified lipids (2D51, 2D60) are introduced downstreamfor processing into consumer products. For example, esterified lipids(2D51) include glyceryl stearate is then mixed with a cannabinoid, thecannabinoid includes one or more selected from the group consisting ofΔ9-tetrahydrocannabinol Δ9-THC, Δ8-tetrahydrocannabinol Δ8-THC,cannabichromene CBC, cannabidiol CBD, cannabigerol CBG, cannabinidiolCBND, and/or cannabinol CBN.

In embodiments, stearic acid is reacted with glycerol to produceglyceryl stearate while in an inert gas environment, the inert gasincludes one or more inert gases selected from the group consisting ofargon, nitrogen, carbon dioxide, air, oxygen, and helium.

In embodiments, a portion of the lipids (1518, 1552), the hydrogenatedlipids (2C58), and/or esterified lipids (2D60) are mixed with oil(2D62), wax (2D63), and the other ingredients (2D64) within a mixingtank (2D70) to create a mixture (2D71). The mixture (2D71) is thenheated with a heat exchanger (2D75) to produce a heated mixture (2D71′)which is then pumped, poured, or transferred into a mold (2D80). In,embodiments the mold (2D80) includes a tube (2D81) to make lip balm. Inembodiments, the heated mixture (2D71′) is pumped into molds (2D80) viaa mixture pump (2D81).

The heat exchanger (2D75) is configured to heat the mixture (2D71)within the mixing tank (2D70) to create a heated mixture (2D71′) at atemperature including one or more temperature ranges selected from thegroup consisting of: 75 degrees Fahrenheit to 100 degrees Fahrenheit,100 degrees Fahrenheit to 125 degrees Fahrenheit, 125 degrees Fahrenheitto 150 degrees Fahrenheit, 150 degrees Fahrenheit to 175 degreesFahrenheit, 175 degrees Fahrenheit to 200 degrees Fahrenheit, 200degrees Fahrenheit to 225 degrees Fahrenheit, 225 degrees Fahrenheit to250 degrees Fahrenheit, 250 degrees Fahrenheit to 275 degreesFahrenheit, 275 degrees Fahrenheit to 300 degrees Fahrenheit, 300degrees Fahrenheit to 325 degrees Fahrenheit, 325 degrees Fahrenheit to350 degrees Fahrenheit.

In embodiments, the mold (2D80) is a tube that includes an open top(3DT) and a closed bottom (3DB) that are spaced apart along a verticalaxis (3DV). The mold (2D80) has a vertical axis (3DV) and a horizontalaxis (3DH). In embodiments, the range of height of the mold (2D80) isselected from one or more from the group consisting of 15 millimeters to17 millimeters, 17 millimeters to 19 millimeters, 19 millimeters to 21millimeters, 21 millimeters to 23 millimeters, 23 millimeters to 25millimeters, 25 millimeters to 27 millimeters, 27 millimeters to 29millimeters, 29 millimeters to 31 millimeters, 31 millimeters to 33millimeters, 33 millimeters to 35 millimeters, 35 millimeters to 37millimeters, 37 millimeters to 39 millimeters, 39 millimeters to 41millimeters, 41 millimeters to 43 millimeters, 43 millimeters to 45millimeters, 45 millimeters to 47 millimeters, 47 millimeters to 49millimeters, 49 millimeters to 51 millimeters, 51 millimeters to 53millimeters, 53 millimeters to 55 millimeters, 55 millimeters to 57millimeters, 57 millimeters to 59 millimeters, 59 millimeters to 61millimeters, 61 millimeters to 63 millimeters, 63 millimeters to 65millimeters, 65 millimeters to 67 millimeters, 67 millimeters to 69millimeters, 69 millimeters to 71 millimeters, and 71 millimeters to 73millimeters.

In embodiments, the range of diameter of the tubular mold (2D80) isselected from one or more from the group consisting of 5 millimeters to6 millimeters, 6 millimeters to 7 millimeters, 7 millimeters to 8millimeters, 8 millimeters to 9 millimeters, 9 millimeters to 10millimeters, 10 millimeters to 11 millimeters, 11 millimeters to 12millimeters, 12 millimeters to 13 millimeters, 13 millimeters to 14millimeters, 14 millimeters to 15 millimeters, 15 millimeters to 16millimeters, 16 millimeters to 17 millimeters, 17 millimeters to 18millimeters, 18 millimeters to 19 millimeters, 19 millimeters to 20millimeters, 20 millimeters to 21 millimeters, 21 millimeters to 22millimeters, 22 millimeters to 23 millimeters, 23 millimeters to 24millimeters, 24 millimeters to 25 millimeters, and 25 millimeters to 26millimeters.

In embodiments, the mold (2D80) contains a volume of the mixture (2D71,2D71′) is selected from one or more from the group consisting of 0.50milliliters to 0.75 milliliters, 0.75 milliliters to 1.00 milliliters,1.00 milliliters to 1.25 milliliters, 1.25 milliliters to 1.50milliliters, 1.50 milliliters to 1.75 milliliters, 1.75 milliliters to2.00 milliliters, 2.00 milliliters to 2.25 milliliters, 2.25 millilitersto 2.50 milliliters, 2.50 milliliters to 2.75 milliliters, 2.75milliliters to 3.00 milliliters, 3.00 milliliters to 3.25 milliliters,3.25 milliliters to 3.50 milliliters, 3.50 milliliters to 3.75milliliters, 3.75 milliliters to 4.00 milliliters, 4.00 milliliters to4.25 milliliters, 4.25 milliliters to 4.50 milliliters, 4.50 millilitersto 4.75 milliliters, 4.75 milliliters to 5.00 milliliters, 5.00milliliters to 5.25 milliliters, 5.25 milliliters to 5.50 milliliters,5.50 milliliters to 5.75 milliliters, 5.75 milliliters to 6.00milliliters, 6.00 milliliters to 6.25 milliliters, 6.25 milliliters to6.50 milliliters, 6.50 milliliters to 6.75 milliliters, 6.75 millilitersto 7.00 milliliters, 7.00 milliliters to 7.25 milliliters, 7.25milliliters to 7.50 milliliters, 7.50 milliliters to 7.75 milliliters,and 7.75 milliliters to 8.00 milliliters.

In embodiments, the mold (2D80) is a material including one or morematerials selected from the group consisting of plastic. In embodiments,the mold (2D80) is transparent, white, black, green, or not transparent.In embodiments, the mold (2D80) is translucent. In embodiments, the mold(2D80) includes a label (2D91) and an adhesive (2D92) for advertisingthe Insectergy® registered trademark or Energy Insects® registeredtrademark.

In embodiments, the esterified lipids (2D51) is then mixed with an oil(2D62), the oil (2D62) includes one or more oils selected from the groupconsisting of a cannabinoid, lipids extracted from insects, almond oil,animal-based oils, apricot kernel oil, avocado oil, brazil nut oil,butter, canola oil, cashew oil, cocoa butter, coconut oil, cooking oil,coffee oil, corn oil, cottonseed oil, fish oil, grapeseed oil, hazelnutoil, hemp oil, hop oil. insect oil, lard, lard oil, macadamia nut oil,mustard oil, olive oil, palm kernel oil, palm oil, peanut oil,peppermint oil, rapeseed oil, rice oil, rice bran oil, safflower oil,semi-refined sesame oil, semi-refined sunflower oil, sesame oil, soybeanoil, tallow of beef, tallow of mutton, vegetable oil, and walnut oil.

In embodiments, the esterified lipids (2D51) is then mixed with a wax(2D63), the wax (2D63) includes, cannabis wax (as described in Volume IIbelow), acacia decurrens flower cera (mimosa flower wax), almond wax,avocado wax, beery wax, bees wax, cananga odorata flower cera (ylangylang flower wax), candelilla wax, Cannabis sativa oil, castor wax,cupuacu butter, floral wax, hemp wax, hydrogenated almond oil,hydrogenated animal-based oils, hydrogenated apricot kernel oil,hydrogenated avocado oil, hydrogenated brazil nut oil, hydrogenatedcanola oil, hydrogenated cashew oil, hydrogenated cocoa butter,hydrogenated coconut oil, hydrogenated coffee oil, hydrogenated cornoil, hydrogenated cottonseed oil, hydrogenated grapeseed oil,hydrogenated hazelnut oil, hydrogenated hemp oil, hydrogenated hop oil,hydrogenated insect oil, hydrogenated lard oil, hydrogenated lard,hydrogenated macadamia nut oil, hydrogenated mustard oil, hydrogenatedolive oil, hydrogenated palm kernel oil, hydrogenated palm oil,hydrogenated peanut oil, hydrogenated peppermint oil, hydrogenatedrapeseed oil, hydrogenated rice bran oil, hydrogenated rice oil,hydrogenated safflower oil, hydrogenated semi-refined sesame oil,hydrogenated semi-refined sunflower oil, hydrogenated sesame oil,hydrogenated soybean oil, hydrogenated walnut oil, jasminum grandiflorumflower cera (jasmine flower wax), Lavandula angustifolia flower cera(lavender flower wax), mmyrica fruit wax, olive wax, prunus amygdalusdulcis oil, rapeseed wax, rice bran wax, rosa damascene flower cera(rose flower wax), shea butter, soybean wax, sunflower wax, vegan wax,vegetable wax, wax from Mexican shrub Euphorbia antisyphilitica, and waxfrom the berries of rhus verniciflua.

In embodiments, the esterified lipids (2D51) is then mixed with one ormore ingredients (2D64) selected from the group consisting of allspiceberries, almond meal, anise seed, annato seed, arrowroot powder, basil,bay leaves, black pepper, buttermilk, capsaicin, caraway, cayenne,celery seed, cheese cultures, chervil, chile powder, chives, cilantro,cinnamon, citric acid, cloves, coconut shredded, coriander, corn oil,corn starch, cream of tartar, cubeb berries, cumin, curry, dextrose,dill, enzymes, fennel, fenugreek, file powder, garlic powder, ginger,grapefruit peel, green peppercorns, honey, horseradish powder, juniperberries, kaffir lime, lavender, lemon grass powder, lemon peel, limepeel, long pepper, marjoram, molasses, mustard, natural smoke flavor,nigella seeds, nutmeg, onion powder, orange peel, oregano, paprika,parsley, peppermint, poppy seed, powdered cheese, red pepper, rosepetals, rosemary, saffron, sassafrass, sage, salt, savory, sesame seed,star anise, sugar, sugar maple, sumac, tamarind, tangerine peel,tarragon, thyme, tomatillo powder, tomato powder, turmeric, vanillaextract, wasabi powder, whey, and white peppercorns.

In embodiments, the esterified lipids (2D51) is then mixed with one ormore ingredients (2D64) selected from the group consisting of ayahuasca,biologically active organic compound with four rings, a nootropic drug,acetate, activated charcoal, an amphetamine, ascorbic acid, aspirin,butyrate, calcium, cannabinoids, cannabinoid drugs, water soluble powdercannabinoid drugs, liquid cannabinoid drugs, capsaicin, carnitine,carnosine, cassia cinnamon, chondroitin sulfate, chromium, coenzymeq-10, cranberry, creatine, curcumin, deprenyl, dimethyltryptamine,echinacea, fish oil, garlic, ginger, ginkgo, ginseng, gluconic acid,glucosamine, green tea, hoodia, human growth hormone,7-hydroxymitragynine, inositol, iowaska, kratom, lactic acid, lithium,lion's mane mushroom, lutein, magnesium, minerals, malate, melatonin,metformin, 3,4-methylenedioxymethamphetamine, milk thistle,n-acetylcysteine, niacin, niacinamide, nicotinamide riboside, omega-3fatty acid, oxaloacetate, piracetam, psilocybin, pyruvate, resveratrol,rhodiola, saw palmetto, selenium, St. john's wort, steroid alternatives,steroids, testosterone, theaflavins, turmeric, valerian, vitamins,vitamin B3, vitamin C, and zinc.

In embodiments, the esterified lipids (2D51) is then mixed with one ormore ingredients (2D64) selected from the group consisting of serotonin,psilocybin, psilocin, baeocystin, norbaeocystin, lysergic aciddiethylamide (LSD), mescaline.

In embodiments, fungi growing within the Farming Superstructure System(FSS) includes psilocybin mushrooms. In embodiments, the FarmingSuperstructure System (FSS) grows psilocybin mushrooms. In embodiments,fungi growing within the Insect Production Superstructure System (IPSS)includes psilocybin mushrooms. In embodiments, the FarmingSuperstructure System (FSS) grows mushrooms. In embodiments, fungigrowing within the Insect Production Superstructure System (IPSS)includes mushrooms. In embodiments, the Insect Production SuperstructureSystem (IPSS) grows psilocybin mushrooms. In embodiments, fungi growingwithin the Insect Production Superstructure System (IPSS) includespolyphyletic fungi. In embodiments, the Insect Production SuperstructureSystem (IPSS) grows polyphyletic fungi.

It is common for people to refer to psilocybin mushrooms as shrooms,psychedelic mushrooms, or magic mushrooms. In embodiments, thepsilocybin mushrooms include a mycelium, stalk, and a cap. Inembodiments, the mycelium contains a psilocybin content in weightpercent ranging from 0.05 to 0.10, 0.10 to 0.15, 0.15 to 0.20, 0.20 to0.25, 0.25 to 0.30, 0.30 to 0.35, 0.35 to 0.40, 0.40 to 0.45, 0.45 to0.50, 0.50 to 0.55, 0.55 to 0.60, 0.60 to 0.65, 0.65 to 0.70, 0.70 to0.75, 0.75 to 0.80, 0.80 to 0.85, 0.85 to 0.90, 0.90 to 0.95, and 0.95to 1.00. For example, the mycelium contains a psilocybin content inweight percent ranging from 0.20 to 0.40. For example, the myceliumcontains a psilocybin content in weight percent ranging from 0.35 to0.55.

In embodiments, the dried cap of the psilocybin mushroom contains apsilocybin content in weight percent ranging from 0.25 to 0.35, 0.35 to0.45, 0.45 to 0.55, 0.55 to 0.65, 0.65 to 0.75, 0.75 to 0.85, 0.85 to0.95, 0.95 to 1.05, 1.05 to 1.15, 1.15 to 1.25, 1.25 to 1.35, 1.35 to1.45, 1.45 to 1.55, 1.55 to 1.65, 1.65 to 1.75, 1.75 to 1.85, 1.85 to1.95, 1.95 to 2.05, and 2.05 to 2.15. For Example, the dried cap of thepsilocybin mushroom contains a psilocybin content in weight percentranging from 0.20 to 0.60. For Example, the dried cap of the psilocybinmushroom contains a psilocybin content in weight percent ranging from0.40 to 0.80. For Example, the dried cap of the psilocybin mushroomcontains a psilocybin content in weight percent ranging from 0.70 to1.1. For Example, the dried cap of the psilocybin mushroom contains apsilocybin content in weight percent ranging from 1.0 to 1.55. ForExample, the dried cap of the psilocybin mushroom contains a psilocybincontent in weight percent ranging from 1.55 to 2.15.

In embodiments, the psilocybin mushrooms include a mycelium, stalk, anda cap. In embodiments, the cap of the psilocybin mushroom has relativelymore psilocybin, baeocystin, and/or norbaeocystin when compared to thestalk. In embodiments, the cap of the psilocybin mushroom has relativelymore psilocybin, baeocystin, and/or norbaeocystin when compared to themycelium.

The mycelium grows in a sterile and/or sterilized breeding material (asseen herein in Volume I: Insect Production Superstructure System (IPSS))and also within the growing medium (as seen below in Volume II: FarmingSuperstructure System (FSS)).

In embodiments, the growing medium within Volume II: FarmingSuperstructure System (FSS) is heated to produce a sterile and/orsterilized growing medium for the psilocybin mushrooms and/or thecannabis plants to grow in.

The mycelium grows in a breeding material and spreads throughout thebreeding material consuming nutrients so as to effectuate the growth ofthe stalk and then the cap (as seen herein in Volume I: InsectProduction Superstructure System (IPSS))

The mycelium grows in a growing medium and spreads throughout thegrowing medium (in either the first growing medium (cloning) or secondgrowing medium (plant growth from young to adult plants) also consumingnutrients so as to effectuate the growth of the stalk and then the cap(as seen herein in Volume II: Farming Superstructure System (FSS).

The mycelium grows in a breeding material (as seen herein in Volume I:Insect Production Superstructure System (IPSS)) and also within thegrowing medium (as seen below in Volume II: Farming SuperstructureSystem (FSS)).

Psilocybin mushrooms have benefits when mixed with cannabinoids orinsect lipids. The cannabinoids have a synergistic affect upon the userfor a more upbeat and positive experience. The insect lipids allow forfast drug delivery in either a tincture (placed under the tongue for 30seconds), a beverage, softgel, water-soluble crystal, emulsion,foodstuff, injectable, and other disclosed methods and possibilitieswith any other ingredient listed in this specification.

Insect lipids offer great promise as a drug delivery agent due to itsunique ability of the arthropod fatty acid to penetrate membrane surfaceas compared to plant-based or mammal-based fatty acids. The insect lipiddrug delivery is one of the most promising aspect of twenty-firstcentury technology since it can be applied to a fat source for animalsand humans as a carrier for a pharmaceutical or other chemicalcompounds, and in biosensors for medical devices, smartphones,nanotechnology medical diagnostic systems, biosensors, fitness watches,to fitness bracelet biosensors, fitness biosensors, and the like. Inembodiments, the insect lipids are used to extract cannabinoids fromcannabis plants.

It is preferable to grow psilocybin mushrooms in the waste of insects.It is preferable to grow psilocybin mushrooms in the waste of cannabisplants. It is preferable to grow psilocybin mushrooms in the waste ofinsects or animals that eat cannabis waste. It is preferable to growpsilocybin mushrooms in the waste of insects or animals that food waste.It is preferable to grow psilocybin mushrooms in the waste of crickets.It is preferable to grow psilocybin mushrooms in the waste of blacksoldier fly larvae. It is preferable to grow psilocybin mushrooms in thewaste of bats. It is preferable to grow psilocybin mushrooms in thewaste of cows. It is preferable to grow psilocybin mushrooms in thewaste of mammals. It is preferable to grow psilocybin mushrooms in thewaste of fish. It is preferable to grow psilocybin mushrooms in thewaste of humans. It is preferable to grow psilocybin mushrooms in thewaste of beetles. It is preferable to grow psilocybin mushrooms in thewaste of arthropods.

In embodiments, the Insect Production Superstructure System (IPSS) growsmushrooms. In embodiments, the Farming Superstructure System (FSS) growsand processes psilocybin mushrooms while growing the psilocybinmushrooms together with cannabis plants. In embodiments, the FarmingSuperstructure System (FSS) grows and processes psilocybin mushroomswhile growing the psilocybin mushrooms together with plants. Inembodiments, the feeding or breeding chambers of the Insect ProductionSuperstructure System (IPSS) grows psilocybin mushrooms.

In embodiments, any of the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may be derived from psilocybin mushrooms. In embodiments,the psilocybin mushrooms grown within the Farming Superstructure System(FSS) includes psilocybin, psilocin, baeocystin, and/or norbaeocystin.In embodiments, the psilocybin mushrooms grown within the InsectProduction Superstructure System (IPSS) includes psilocybin, psilocin,baeocystin, and/or norbaeocystin. In embodiments, any of the psilocybin,psilocin, baeocystin, and/or norbaeocystin may be derived frompsilocybin mushrooms. In embodiments, the psilocybin mushrooms grownwithin the Farming Superstructure System (FSS) includes psilocybin,psilocin, and not baeocystin. In embodiments, the psilocybin mushroomsgrown within the Insect Production Superstructure System (IPSS) includespsilocybin, psilocin, and not baeocystin.

In embodiments, any of the psilocybin, psilocin, and/or baeocystin maybe derived from psilocybin mushrooms. In embodiments, the psilocybinmushrooms grown within the Farming Superstructure System (FSS) includespsilocybin, and not psilocin and baeocystin. In embodiments, thepsilocybin mushrooms grown within the Insect Production SuperstructureSystem (IPSS) includes psilocybin, and not psilocin and baeocystin.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes one or more of psilocybin, psilocin, baeocystin,norbaeocystin, salts thereof, or combinations thereof. In embodiments,the psilocybin mushrooms and/or the alimentary composition includes oneor more of erinacines, hericenones or combinations thereof, and niacin.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes one or more of alpha-tocopherol, ascorbic acid,biotin, caffeine, calciferol, calcium, carotene, chloride, choline,chromium, citicoline, cobalamin, copper, fluoride, folacin, folate,folic acid, glucuronic acid, iodine, iron, L-phenylalanine, magnesium,malic acid, manganese, menadione, mineral, molybdenum, N-acetyl Ltyrosine, niacin, pantothenic acid, phosphorus, phylloquinone,potassium, pyridoxine, retinal, retinoic acid, retinoids, retinol,retinyl esters, riboflavin, selenium, sodium, sulfur, taurine, thiamine,Vitamin A, Vitamin B1, vitamin B12, Vitamin B2, vitamin B3, vitamin B5,vitamin B6, vitamin B9, vitamin C, vitamin D, Vitamin E, vitamin H,vitamin K, or zinc.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes one or more of ayahuasca, biologically activeorganic compound with four rings, a nootropic drug, acetate, activatedcharcoal, an amphetamine, ascorbic acid, aspirin, butyrate, calcium,capsaicin, carnitine, carnosine, cassia cinnamon, chondroitin sulfate,chromium, coenzyme q-10, cranberry, creatine, curcumin, deprenyl,dimethyltryptamine, echinacea, fish oil, garlic, ginger, ginkgo,ginseng, gluconic acid, glucosamine, green tea, hoodia, human growthhormone, 7-hydroxymitragynine, inositol, iowaska, kratom, lactic acid,lithium, lion's mane mushroom, lutein, magnesium, minerals, malate,melatonin, metformin, 3,4-methylenedioxymethamphetamine, milk thistle,n-acetylcysteine, niacin, niacinamide, nicotinamide riboside, omega-3fatty acid, oxaloacetate, piracetam, psilocybin, pyruvate, resveratrol,rhodiola, saw palmetto, selenium, St. john's wort, steroid alternatives,steroids, testosterone, theaflavins, turmeric, valerian.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes one or more of basil, bergamot, black pepper,cassia, cedarwood, cinnamon, citronella, clary sage, clove, coffee,cypress, eucalyptus, evening primrose, fennel, fir needle, frankincense,gardenia, geranium, ginger, grapefruit, helichrysum, hop, hyssop,jasmine, juniper berry, lavender, lemon, lemongrass, mandarin, marjoram,melaleuca, melissa, myrrh, neroli, orange, oregano, palo santo,patchouli, peppermint, pine, roman chamomile, rose, rosemary,sandalwood, spikenard, tea tree, thyme, turmeric, vetiver, wintergreen,and ylang ylang.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes one or more of barley, binding agents, brown rice,buckwheat flour, buckwheat, bulgur, carrageenan, corn meal, corn,cracked wheat, cricket flour, density improving textural supplements,farro, fiber-starch materials, insect flour, insects, mealworms, millet,moisture improving textural supplements, oatmeal, popcorn, quinoa, rice,rye, sorghum, triticale, wheat, whole farro, whole grain barley, wholegrain corn, whole oats, whole rye, whole wheat flour, wild rice,fiber-starch materials, binding agents, density improving texturalsupplements, and moisture improving textural supplements.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes an emulsifier selected from the group consisting ofa surfactant, a nonionic surfactant, lecithin, polyethylene (40),stearate, polysorbate, Polyoxyethylene sorbitan monooleate,Polyoxyethylene (20) sorbitan monooleate, polysorbate 80, polysorbate60, polysorbate 65, ammonium salts of phosphatidic acid, sucrose acetateisobutyrate, potassium pyrophosphate, sodium acid pyrophosphate, sodiumpyrophosphate, potassium polymetaphosphate, sodium metaphosphate,insoluble or sodium polyphosphates, sodium polyphosphates, insolublepolyphosphates, glassy salts of fatty acids, mono- and di-glycerides offatty acids, mono-glycerides of fatty acids, di-glycerides of fattyacids, acetic and fatty acid esters of glycerol, lactic and fatty acidesters of glycerol, citric and fatty acid esters of glycerol,diacetyltartaric and fatty acid esters of glycerol, mixed fatty acidesters of glycerol, sucrose esters of fatty acids, polyglycerol estersof fatty acids, polyglycerol esters of interesterified ricinoleic acid,propylene glycol mono- and di-esters, propylene glycol di-esters,propylene glycol mono-esters, propylene glycol esters of fatty acids,propylene glycol esters, dioctyl sodium sulphosuccinate, sodiumlactylate, sodium oleyl lactylate, sodium stearoyl lactylate, calciumlactylate, calcium oleyl lactylate, calcium stearoyl lactylate, sorbitanmonostearate, maltodextrin, polyphosphates, formulated polyphosphates,and gum arabic.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes treated water. In embodiments, the psilocybinmushrooms and/or the alimentary composition includes a microorganism,bacteria, fungi, Lactobacilli, Lactobacillus acidophilus, Lactobacillusbulgaricus, Lactobacillus plantarum, Lactobacillus rhamnosus,Lactobacillus fermentum, Lactobacillus caucasicus, Lactobacillushelveticus, Lactobacillus lactis, Lactobacillus reuteri, Lactobacilluscasei, Lactobacillus brevis, Lactobacillus gasseri, Lactobacillusparacasei, Lactobacillus salivarius, Bifidobacteria, Bifidobacteriumanimalis, Bifidobacterium bifidum, Bifidobacterium breve,Bifidobacterium infantis, Bifidobacterium lactis, Bifidobacteriumlongum, Enterococcus faecium, Streptococcus thermophilus, Bacilluslaterosporus, and Pediococcus acidilactici.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition be further processed to create foodstuffs not only includingada, bagels, baked goods, biscuits, bitterballen, bonda, breads, cakes,candies, cereals, chips, chocolate bars, chocolate, coffee, cokodok,confectionery, cookies, cooking batter, corn starch mixtures, crackers,crêpes, croissants, croquettes, croutons, dolma, dough, doughnuts,energy bars, flapjacks, french fries, frozen custard, frozen desserts,frying cakes, fudge, gelatin mixes, granola bars, gulha, hardtack, icecream, khandvi, khanom buang, krumpets, meze, mixed flours, muffins,multi-grain snacks, nachos, nian gao, noodles, nougat, onion rings,pakora, pancakes, panforte, pastas, pastries, pie crust, pita chips,pizza, poffertjes, pretzels, protein powders, pudding, rice krispietreats, sesame sticks, smoothies, snacks, specialty milk, tele-bhaja,tempura, toffee, tortillas, totopo, turkish delights, or waffles.

In embodiments, the fiber-starch materials may be comprised of singularor mixtures of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, or vegetable-based materials. In embodiments, thebinding agents may be comprised of singular or mixtures of agar, agave,alginin, aspartame, arrowroot, carrageenan, collagen, cornstarch, eggwhites, finely ground seeds, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, proteins,psyllium husks, sago, sugars, stevia, syrups, tapioca, vegetable gums,or xanthan gum. In embodiments, the moisture improving texturalsupplements may be comprised of singular or mixtures of almonds, brazilnuts, cacao, cashews, chestnuts, coconut, filberts, hazelnuts, Indiannuts, macadamia nuts, nut butters, nut oils, nut powders, peanuts,pecans, pili nuts, pine nuts, pinon nuts, pistachios, soy nuts,sunflower seeds, tiger nuts, walnuts, and oils extracted from any one ofthe aforesaid nuts and nuts listed herein and combinations thereof. Inembodiments, the insects may be Orthoptera order of insects includinggrasshoppers, crickets, cave crickets, Jerusalem crickets, katydids,weta, lubber, acrida, and locusts. However, other orders of insects,such as cicadas, ants, mealworms, agave worms, worms, bees, centipedes,cockroaches, dragonflies, beetles, scorpions, tarantulas, and termitesmay be used as well.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition is administered to a human and/or an animal. In embodiments,the psilocybin mushrooms and/or the alimentary composition. improvesmemory and cognition, motor skills and coordination, the ability tosolve complex computer coding challenges, hearing, vision, sensoryfunction, learning, or neurogenesis.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises one or more of (Bacopa monnieri), Gotu kola(Centella asiatica), Gingko (Gingko biloba), Ginger (Zingiberofficinale), Holy Basil (Ocimum sanctum), Hu Zhang (Polygonumcuspidatum), Oregano (Origanum vulgare, Origanum onites), Rosemary(Rosmarinus officinalis, Rosmarinus eriocalyx, Rosmarinus species),Turmeric (Curcuma longa), Green Tea (Camellia sinensis), lavender(Lavandula spica and Lavandula species), skullcap (Scutellarialateriflora), oat straw (Avena sativa and Avena byzantine), Diviner'sSage (Salvia divinorum), ayahuasca (Banisteriopsis caapi and Psychotriaspecies), Tabernanthe iboga, Voacanga africana, Tabernaemontanaundulate, peyote (Lophophora williamsii), morning glory (Ipomoeatricolor, Argyreia nervosa), Cannabis sativa, Cannabis indica orCannabis ruderalis, or combinations thereof.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises one or more mycelium of Antrodia, Beauveria,Copelandia, Cordyceps, Ganoderma, Grifola, Hericium, Inonotus, Isaria,Panaeolus or Phellinus fungi, or combinations thereof; one or moreextract of mycelium of Antrodia, Beauveria, Copelandia, Cordyceps,Ganoderma, Grifola, Hericium, Inonotus, Isaria Panaeolus or Phellinus,or combinations; one or more extract of Antrodia, Beauveria, Copelandia,Cordyceps, Ganoderma, Grifola, Hericium, Inonotus, Isaria, Panaeolus orPhellinus fruitbodies, or combinations thereof; or combinations thereof.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises a dose of a composition for at least one month toa patient, wherein the composition comprises: one or more of about 0.1to 10 mg of psilocybin, psilocin, baeocystin, norbaeocystin, or saltsthereof, one or more of about 0.1 to 1 gram of psilocybin mushrooms, orcombinations thereof; about 0.1 to 200 mg of one or more of erinacines,hericenones, or combinations thereof; and about 1 to 200 mg of niacin.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises a dose of about 0.6 to 10 mg of one or more ofpsilocybin, psilocin, baeocystin, norbaeocystin, salts thereof, orcombinations thereof, about 20 to 200 mg of one or more of erinacines,hericenones, or combinations thereof, and about 50 to 200 mg of niacin.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises a dose of about 0.9 to 10 mg of one or more ofpsilocybin, psilocin, baeocystin, norbaeocystin, salts thereof, orcombinations thereof, about 50 to 200 mg of one or more of erinacines,hericenones, or combinations thereof, and about 50 to 200 mg of niacin.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises one or more of (Bacopa monnieri), Gotu kola(Centella asiatica), Gingko (Gingko biloba), Ginger (Zingiberofficinale), Holy Basil (Ocimum sanctum), Hu Zhang (Polygonumcuspidatum), Oregano (Origanum vulgare, Origanum onites), Rosemary(Rosmarinus officinalis, Rosmarinus eriocalyx, Rosmarinus species),Turmeric (Curcuma longa), Green Tea (Camellia sinensis), lavender(Lavandula spica and Lavandula species), skullcap (Scutellarialateriflora), oat straw (Avena sativa and Avena byzantine), Diviner'sSage (Salvia divinorum), ayahuasca (Banisteriopsis caapi and Psychotriaspecies), Tabernanthe iboga, Voacanga africana, Tabernaemontanaundulate, peyote (Lophophora williamsii), morning glory (Ipomoeatricolor, Argyreia nervosa), Cannabis sativa, Cannabis indica orCannabis ruderalis, or combinations thereof.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition comprises one or more of erinacines, hericenones, orcombinations thereof; niacin; and one or more of N,N-dimethyltryptamine,5-hydroxytryptamine, 5-hydroxytryptophan,4-acetoxy-N,N-dimethyltryptamine, 4-acetoxy-N-methyl-N-ethyltryptamine,4-acetoxy-N,N-diethyltryptamine, 4-acetoxy-N-methyl-N-propyltryptamine,4-acetoxy-N-methyl-N-isopropyltryptamine,4-acetoxy-N,N-dipropyltryptamine, 4-acetoxy-N,N-diisopropyltryptamine,4-hydroxy-N-methyl-N-ethyltryptamine,4-hydroxy-N-methyl-N-propyltryptamine,4-hydroxy-N-methyl-N-isopropyltryptamine,4-hydroxy-N,N-diisopropyltryptamine,4-hydroxy-N,N-diisopropyltryptamine,4-hydroxy-N-methyl-N-propyltryptamine, 4-hydroxy-N,N-diethyltryptamine,4-hydroxy-N,N-diallyltryptamine, N-methyl-N-ethyltryptamine,N,N-diethyltryptamine, N,N-dipropyltriptamine,N,N-diisopropyltryptamine, N-methyl-N-propyltryptamine,N-methyl-N-isopropyltryptamine, a-methyl-tryptamine,N-ethyl-N-isopropyltryptamine, N-methyl-N-butyl-tryptamine,N,N-dimethyl-5-hydroxytryptamine, 5-methoxy-a-methyltryptamine,5-methoxy-N,N-dimethyltryptamine, 5-methoxy-N,N-diethyltryptamine,5-methoxy-N,N-dipropyltryptamine, 5-methoxy-N,N-diisopropyltryptamine,5-methoxy-N-ethyl-N-isopropyltryptamine, 2,a-dimethyltryptamine,a,N-dimethyltryptamine, a-ethyltryptamine,2-methyl-N,N-dimethyltryptamine, 2-methyl-N,N-diethyltryptamine,1-methylpsilocin, ibogaine, 4-hydroxindole-3-acetylaldehyde,4-hydroxtryptophol, 4-hydroxindole-3-acetic acid, salts thereof, orcombinations thereof.

In embodiments, the psilocybin content within the psilocybin mushroomsranges from one or more weight percentages selected from the group ofconsisting of: 0.00 weight percent to 0.05 weight percent, 0.05 weightpercent to 0.10 weight percent, 0.10 weight percent to 0.15 weightpercent, 0.15 weight percent to 0.20 weight percent, 0.20 weight percentto 0.25 weight percent, 0.25 weight percent to 0.30 weight percent, 0.30weight percent to 0.35 weight percent, 0.35 weight percent to 0.40weight percent, 0.40 weight percent to 0.45 weight percent, 0.45 weightpercent to 0.50 weight percent, 0.50 weight percent to 0.55 weightpercent, 0.55 weight percent to 0.60 weight percent, 0.60 weight percentto 0.65 weight percent, 0.65 weight percent to 0.70 weight percent, 0.70weight percent to 0.75 weight percent, 0.75 weight percent to 0.80weight percent, 0.80 weight percent to 0.85 weight percent, 0.85 weightpercent to 0.90 weight percent, 0.90 weight percent to 0.95 weightpercent, 0.95 weight percent to 1.00 weight percent, 1.00 weight percentto 1.05 weight percent, 1.05 weight percent to 1.10 weight percent, 1.10weight percent to 1.15 weight percent, 1.15 weight percent to 1.20weight percent, 1.20 weight percent to 1.25 weight percent, 1.25 weightpercent to 1.30 weight percent, 1.30 weight percent to 1.35 weightpercent, 1.35 weight percent to 1.40 weight percent, 1.40 weight percentto 1.45 weight percent, 1.45 weight percent to 1.50 weight percent, 1.50weight percent to 1.55 weight percent, 1.55 weight percent to 1.60weight percent, 1.60 weight percent to 1.65 weight percent, 1.65 weightpercent to 1.70 weight percent, 1.70 weight percent to 1.75 weightpercent, 1.75 weight percent to 1.80 weight percent, 1.80 weight percentto 1.85 weight percent, 1.85 weight percent to 1.90 weight percent, 1.90weight percent to 1.95 weight percent, 1.95 weight percent to 2.00weight percent, 2.00 weight percent to 2.05 weight percent, 2.05 weightpercent to 2.10 weight percent, 2.10 weight percent to 2.15 weightpercent, 2.15 weight percent to 2.20 weight percent, 2.20 weight percentto 2.25 weight percent, 2.25 weight percent to 2.30 weight percent, 2.30weight percent to 2.35 weight percent, 2.35 weight percent to 2.40weight percent, 2.40 weight percent to 2.45 weight percent, 2.45 weightpercent to 2.50 weight percent, 2.50 weight percent to 2.55 weightpercent, 2.55 weight percent to 2.60 weight percent, 2.60 weight percentto 2.65 weight percent, 2.65 weight percent to 2.70 weight percent, 2.70weight percent to 2.75 weight percent, 2.75 weight percent to 2.80weight percent, 2.80 weight percent to 2.85 weight percent, 2.85 weightpercent to 2.90 weight percent, 2.90 weight percent to 2.95 weightpercent, 2.95 weight percent to 3.00 weight percent, 3.00 weight percentto 3.50 weight percent, 3.50 weight percent to 3.55 weight percent, 3.55weight percent to 3.60 weight percent, 3.60 weight percent to 3.65weight percent, 3.65 weight percent to 3.70 weight percent, 3.70 weightpercent to 3.75 weight percent, 3.75 weight percent to 3.80 weightpercent, 3.80 weight percent to 3.85 weight percent, 3.85 weight percentto 3.90 weight percent, 3.90 weight percent to 3.95 weight percent, 3.95weight percent to 4.00 weight percent, 4.00 weight percent to 4.05weight percent, 4.05 weight percent to 4.10 weight percent, 4.10 weightpercent to 4.15 weight percent, 4.15 weight percent to 4.20 weightpercent, 4.20 weight percent to 4.25 weight percent, 4.25 weight percentto 4.30 weight percent, 4.30 weight percent to 4.35 weight percent, 4.35weight percent to 4.40 weight percent, 4.40 weight percent to 4.45weight percent, 4.45 weight percent to 4.50 weight percent, 4.50 weightpercent to 4.55 weight percent, 4.55 weight percent to 4.60 weightpercent, 4.60 weight percent to 4.65 weight percent, 4.65 weight percentto 4.70 weight percent, 4.70 weight percent to 4.75 weight percent, 4.75weight percent to 4.80 weight percent, 4.80 weight percent to 4.85weight percent, 4.85 weight percent to 4.90 weight percent, 4.90 weightpercent to 4.95 weight percent, 4.95 weight percent to 5.00 weightpercent, 5.00 weight percent to 5.05 weight percent, 5.05 weight percentto 5.10 weight percent, 5.10 weight percent to 5.15 weight percent, 5.15weight percent to 5.20 weight percent, 5.20 weight percent to 5.25weight percent, 5.25 weight percent to 5.30 weight percent, 5.30 weightpercent to 5.35 weight percent, 5.35 weight percent to 5.40 weightpercent, 5.40 weight percent to 5.45 weight percent, 5.45 weight percentto 5.50 weight percent, 5.50 weight percent to 5.55 weight percent, 5.55weight percent to 5.60 weight percent, 5.60 weight percent to 5.65weight percent, 5.65 weight percent to 5.70 weight percent, 5.70 weightpercent to 5.75 weight percent, 5.75 weight percent to 5.80 weightpercent, 5.80 weight percent to 5.85 weight percent, 5.85 weight percentto 5.90 weight percent, 5.90 weight percent to 5.95 weight percent, 5.95weight percent to 6.00 weight percent, 6.00 weight percent to 6.05weight percent, 6.05 weight percent to 6.10 weight percent, 6.10 weightpercent to 6.15 weight percent, 6.15 weight percent to 6.20 weightpercent, 6.20 weight percent to 6.25 weight percent, 6.25 weight percentto 6.30 weight percent, 6.30 weight percent to 6.35 weight percent, 6.35weight percent to 6.40 weight percent, 6.40 weight percent to 6.45weight percent, 6.45 weight percent to 6.50 weight percent, 6.50 weightpercent to 6.55 weight percent, 6.55 weight percent to 6.60 weightpercent, 6.60 weight percent to 6.65 weight percent, 6.65 weight percentto 6.70 weight percent, 6.70 weight percent to 6.75 weight percent, 6.75weight percent to 6.80 weight percent, 6.80 weight percent to 6.85weight percent, 6.85 weight percent to 6.90 weight percent, 6.90 weightpercent to 6.95 weight percent, 6.95 weight percent to 7.00 weightpercent, 7.00 weight percent to 7.05 weight percent, 7.05 weight percentto 7.10 weight percent, 7.10 weight percent to 7.15 weight percent, 7.15weight percent to 7.20 weight percent, 7.20 weight percent to 7.25weight percent, 7.25 weight percent to 7.30 weight percent, 7.30 weightpercent to 7.35 weight percent, 7.35 weight percent to 7.40 weightpercent, 7.40 weight percent to 7.45 weight percent, 7.45 weight percentto 7.50 weight percent, 7.50 weight percent to 8.00 weight percent, 8.00weight percent to 8.50 weight percent, 8.50 weight percent to 9.00weight percent, 9.00 weight percent to 9.50 weight percent, 9.50 weightpercent to 10.00 weight percent, 10.00 weight percent to 10.50 weightpercent, 10.50 weight percent to 11.00 weight percent, 11.00 weightpercent to 11.50 weight percent, 11.50 weight percent to 12.00 weightpercent, 12.00 weight percent to 12.50 weight percent, 12.50 weightpercent to 13.00 weight percent, 13.00 weight percent to 13.50 weightpercent, 13.50 weight percent to 14.00 weight percent, 14.00 weightpercent to 14.50 weight percent, 14.50 weight percent to 15.00 weightpercent, 15.00 weight percent to 15.50 weight percent, 15.50 weightpercent to 16.00 weight percent, 16.00 weight percent to 16.50 weightpercent, 16.50 weight percent to 17.00 weight percent, 17.00 weightpercent to 17.50 weight percent, 17.50 weight percent to 18.00 weightpercent, 18.00 weight percent to 18.50 weight percent, 18.50 weightpercent to 19.00 weight percent, 19.00 weight percent to 19.50 weightpercent, 19.50 weight percent to 20.00 weight percent, 20.00 weightpercent to 20.50 weight percent, 20.50 weight percent to 21.00 weightpercent, 21.00 weight percent to 21.50 weight percent, 21.50 weightpercent to 22.00 weight percent, and 22.00 weight percent to 22.50weight percent.

In embodiments, the psilocin content within the psilocybin mushroomsranges from one or more weight percentages selected from the group ofconsisting of: 0.00 weight percent to 0.05 weight percent, 0.05 weightpercent to 0.10 weight percent, 0.10 weight percent to 0.15 weightpercent, 0.15 weight percent to 0.20 weight percent, 0.20 weight percentto 0.25 weight percent, 0.25 weight percent to 0.30 weight percent, 0.30weight percent to 0.35 weight percent, 0.35 weight percent to 0.40weight percent, 0.40 weight percent to 0.45 weight percent, 0.45 weightpercent to 0.50 weight percent, 0.50 weight percent to 0.55 weightpercent, 0.55 weight percent to 0.60 weight percent, 0.60 weight percentto 0.65 weight percent, 0.65 weight percent to 0.70 weight percent, 0.70weight percent to 0.75 weight percent, 0.75 weight percent to 0.80weight percent, 0.80 weight percent to 0.85 weight percent, 0.85 weightpercent to 0.90 weight percent, 0.90 weight percent to 0.95 weightpercent, 0.95 weight percent to 1.00 weight percent, 1.00 weight percentto 1.05 weight percent, 1.05 weight percent to 1.10 weight percent, 1.10weight percent to 1.15 weight percent, 1.15 weight percent to 1.20weight percent, 1.20 weight percent to 1.25 weight percent, 1.25 weightpercent to 1.30 weight percent, 1.30 weight percent to 1.35 weightpercent, 1.35 weight percent to 1.40 weight percent, 1.40 weight percentto 1.45 weight percent, 1.45 weight percent to 1.50 weight percent, 1.50weight percent to 1.55 weight percent, 1.55 weight percent to 1.60weight percent, 1.60 weight percent to 1.65 weight percent, 1.65 weightpercent to 1.70 weight percent, 1.70 weight percent to 1.75 weightpercent, 1.75 weight percent to 1.80 weight percent, 1.80 weight percentto 1.85 weight percent, 1.85 weight percent to 1.90 weight percent, 1.90weight percent to 1.95 weight percent, 1.95 weight percent to 2.00weight percent, 2.00 weight percent to 2.05 weight percent, 2.05 weightpercent to 2.10 weight percent, 2.10 weight percent to 2.15 weightpercent, 2.15 weight percent to 2.20 weight percent, 2.20 weight percentto 2.25 weight percent, 2.25 weight percent to 2.30 weight percent, 2.30weight percent to 2.35 weight percent, 2.35 weight percent to 2.40weight percent, 2.40 weight percent to 2.45 weight percent, 2.45 weightpercent to 2.50 weight percent, 2.50 weight percent to 2.55 weightpercent, 2.55 weight percent to 2.60 weight percent, 2.60 weight percentto 2.65 weight percent, 2.65 weight percent to 2.70 weight percent, 2.70weight percent to 2.75 weight percent, 2.75 weight percent to 2.80weight percent, 2.80 weight percent to 2.85 weight percent, 2.85 weightpercent to 2.90 weight percent, 2.90 weight percent to 2.95 weightpercent, 2.95 weight percent to 3.00 weight percent, 3.00 weight percentto 3.50 weight percent, 3.50 weight percent to 3.55 weight percent, 3.55weight percent to 3.60 weight percent, 3.60 weight percent to 3.65weight percent, 3.65 weight percent to 3.70 weight percent, 3.70 weightpercent to 3.75 weight percent, 3.75 weight percent to 3.80 weightpercent, 3.80 weight percent to 3.85 weight percent, 3.85 weight percentto 3.90 weight percent, 3.90 weight percent to 3.95 weight percent, 3.95weight percent to 4.00 weight percent, 4.00 weight percent to 4.05weight percent, 4.05 weight percent to 4.10 weight percent, 4.10 weightpercent to 4.15 weight percent, 4.15 weight percent to 4.20 weightpercent, 4.20 weight percent to 4.25 weight percent, 4.25 weight percentto 4.30 weight percent, 4.30 weight percent to 4.35 weight percent, 4.35weight percent to 4.40 weight percent, 4.40 weight percent to 4.45weight percent, 4.45 weight percent to 4.50 weight percent, 4.50 weightpercent to 4.55 weight percent, 4.55 weight percent to 4.60 weightpercent, 4.60 weight percent to 4.65 weight percent, 4.65 weight percentto 4.70 weight percent, 4.70 weight percent to 4.75 weight percent, 4.75weight percent to 4.80 weight percent, 4.80 weight percent to 4.85weight percent, 4.85 weight percent to 4.90 weight percent, 4.90 weightpercent to 4.95 weight percent, 4.95 weight percent to 5.00 weightpercent, 5.00 weight percent to 5.05 weight percent, 5.05 weight percentto 5.10 weight percent, 5.10 weight percent to 5.15 weight percent, 5.15weight percent to 5.20 weight percent, 5.20 weight percent to 5.25weight percent, 5.25 weight percent to 5.30 weight percent, 5.30 weightpercent to 5.35 weight percent, 5.35 weight percent to 5.40 weightpercent, 5.40 weight percent to 5.45 weight percent, 5.45 weight percentto 5.50 weight percent, 5.50 weight percent to 5.55 weight percent, 5.55weight percent to 5.60 weight percent, 5.60 weight percent to 5.65weight percent, 5.65 weight percent to 5.70 weight percent, 5.70 weightpercent to 5.75 weight percent, 5.75 weight percent to 5.80 weightpercent, 5.80 weight percent to 5.85 weight percent, 5.85 weight percentto 5.90 weight percent, 5.90 weight percent to 5.95 weight percent, 5.95weight percent to 6.00 weight percent, 6.00 weight percent to 6.05weight percent, 6.05 weight percent to 6.10 weight percent, 6.10 weightpercent to 6.15 weight percent, 6.15 weight percent to 6.20 weightpercent, 6.20 weight percent to 6.25 weight percent, 6.25 weight percentto 6.30 weight percent, 6.30 weight percent to 6.35 weight percent, 6.35weight percent to 6.40 weight percent, 6.40 weight percent to 6.45weight percent, 6.45 weight percent to 6.50 weight percent, 6.50 weightpercent to 6.55 weight percent, 6.55 weight percent to 6.60 weightpercent, 6.60 weight percent to 6.65 weight percent, 6.65 weight percentto 6.70 weight percent, 6.70 weight percent to 6.75 weight percent, 6.75weight percent to 6.80 weight percent, 6.80 weight percent to 6.85weight percent, 6.85 weight percent to 6.90 weight percent, 6.90 weightpercent to 6.95 weight percent, 6.95 weight percent to 7.00 weightpercent, 7.00 weight percent to 7.05 weight percent, 7.05 weight percentto 7.10 weight percent, 7.10 weight percent to 7.15 weight percent, 7.15weight percent to 7.20 weight percent, 7.20 weight percent to 7.25weight percent, 7.25 weight percent to 7.30 weight percent, 7.30 weightpercent to 7.35 weight percent, 7.35 weight percent to 7.40 weightpercent, 7.40 weight percent to 7.45 weight percent, 7.45 weight percentto 7.50 weight percent, 7.50 weight percent to 8.00 weight percent, 8.00weight percent to 8.50 weight percent, 8.50 weight percent to 9.00weight percent, 9.00 weight percent to 9.50 weight percent, 9.50 weightpercent to 10.00 weight percent, 10.00 weight percent to 10.50 weightpercent, 10.50 weight percent to 11.00 weight percent, 11.00 weightpercent to 11.50 weight percent, 11.50 weight percent to 12.00 weightpercent, 12.00 weight percent to 12.50 weight percent, 12.50 weightpercent to 13.00 weight percent, 13.00 weight percent to 13.50 weightpercent, 13.50 weight percent to 14.00 weight percent, 14.00 weightpercent to 14.50 weight percent, 14.50 weight percent to 15.00 weightpercent, 15.00 weight percent to 15.50 weight percent, 15.50 weightpercent to 16.00 weight percent, 16.00 weight percent to 16.50 weightpercent, 16.50 weight percent to 17.00 weight percent, 17.00 weightpercent to 17.50 weight percent, 17.50 weight percent to 18.00 weightpercent, 18.00 weight percent to 18.50 weight percent, 18.50 weightpercent to 19.00 weight percent, 19.00 weight percent to 19.50 weightpercent, 19.50 weight percent to 20.00 weight percent, 20.00 weightpercent to 20.50 weight percent, 20.50 weight percent to 21.00 weightpercent, 21.00 weight percent to 21.50 weight percent, 21.50 weightpercent to 22.00 weight percent, and 22.00 weight percent to 22.50weight percent.

In embodiments, the baeocystin content within the psilocybin mushroomsranges from one or more weight percentages selected from the group ofconsisting of: 0.00 weight percent to 0.05 weight percent, 0.05 weightpercent to 0.10 weight percent, 0.10 weight percent to 0.15 weightpercent, 0.15 weight percent to 0.20 weight percent, 0.20 weight percentto 0.25 weight percent, 0.25 weight percent to 0.30 weight percent, 0.30weight percent to 0.35 weight percent, 0.35 weight percent to 0.40weight percent, 0.40 weight percent to 0.45 weight percent, 0.45 weightpercent to 0.50 weight percent, 0.50 weight percent to 0.55 weightpercent, 0.55 weight percent to 0.60 weight percent, 0.60 weight percentto 0.65 weight percent, 0.65 weight percent to 0.70 weight percent, 0.70weight percent to 0.75 weight percent, 0.75 weight percent to 0.80weight percent, 0.80 weight percent to 0.85 weight percent, 0.85 weightpercent to 0.90 weight percent, 0.90 weight percent to 0.95 weightpercent, 0.95 weight percent to 1.00 weight percent, 1.00 weight percentto 1.05 weight percent, 1.05 weight percent to 1.10 weight percent, 1.10weight percent to 1.15 weight percent, 1.15 weight percent to 1.20weight percent, 1.20 weight percent to 1.25 weight percent, 1.25 weightpercent to 1.30 weight percent, 1.30 weight percent to 1.35 weightpercent, 1.35 weight percent to 1.40 weight percent, 1.40 weight percentto 1.45 weight percent, 1.45 weight percent to 1.50 weight percent, 1.50weight percent to 1.55 weight percent, 1.55 weight percent to 1.60weight percent, 1.60 weight percent to 1.65 weight percent, 1.65 weightpercent to 1.70 weight percent, 1.70 weight percent to 1.75 weightpercent, 1.75 weight percent to 1.80 weight percent, 1.80 weight percentto 1.85 weight percent, 1.85 weight percent to 1.90 weight percent, 1.90weight percent to 1.95 weight percent, 1.95 weight percent to 2.00weight percent, 2.00 weight percent to 2.05 weight percent, 2.05 weightpercent to 2.10 weight percent, 2.10 weight percent to 2.15 weightpercent, 2.15 weight percent to 2.20 weight percent, 2.20 weight percentto 2.25 weight percent, 2.25 weight percent to 2.30 weight percent, 2.30weight percent to 2.35 weight percent, 2.35 weight percent to 2.40weight percent, 2.40 weight percent to 2.45 weight percent, 2.45 weightpercent to 2.50 weight percent, 2.50 weight percent to 2.55 weightpercent, 2.55 weight percent to 2.60 weight percent, 2.60 weight percentto 2.65 weight percent, 2.65 weight percent to 2.70 weight percent, 2.70weight percent to 2.75 weight percent, 2.75 weight percent to 2.80weight percent, 2.80 weight percent to 2.85 weight percent, 2.85 weightpercent to 2.90 weight percent, 2.90 weight percent to 2.95 weightpercent, 2.95 weight percent to 3.00 weight percent, 3.00 weight percentto 3.50 weight percent, 3.50 weight percent to 3.55 weight percent, 3.55weight percent to 3.60 weight percent, 3.60 weight percent to 3.65weight percent, 3.65 weight percent to 3.70 weight percent, 3.70 weightpercent to 3.75 weight percent, 3.75 weight percent to 3.80 weightpercent, 3.80 weight percent to 3.85 weight percent, 3.85 weight percentto 3.90 weight percent, 3.90 weight percent to 3.95 weight percent, 3.95weight percent to 4.00 weight percent, 4.00 weight percent to 4.05weight percent, 4.05 weight percent to 4.10 weight percent, 4.10 weightpercent to 4.15 weight percent, 4.15 weight percent to 4.20 weightpercent, 4.20 weight percent to 4.25 weight percent, 4.25 weight percentto 4.30 weight percent, 4.30 weight percent to 4.35 weight percent, 4.35weight percent to 4.40 weight percent, 4.40 weight percent to 4.45weight percent, 4.45 weight percent to 4.50 weight percent, 4.50 weightpercent to 4.55 weight percent, 4.55 weight percent to 4.60 weightpercent, 4.60 weight percent to 4.65 weight percent, 4.65 weight percentto 4.70 weight percent, 4.70 weight percent to 4.75 weight percent, 4.75weight percent to 4.80 weight percent, 4.80 weight percent to 4.85weight percent, 4.85 weight percent to 4.90 weight percent, 4.90 weightpercent to 4.95 weight percent, 4.95 weight percent to 5.00 weightpercent, 5.00 weight percent to 5.05 weight percent, 5.05 weight percentto 5.10 weight percent, 5.10 weight percent to 5.15 weight percent, 5.15weight percent to 5.20 weight percent, 5.20 weight percent to 5.25weight percent, 5.25 weight percent to 5.30 weight percent, 5.30 weightpercent to 5.35 weight percent, 5.35 weight percent to 5.40 weightpercent, 5.40 weight percent to 5.45 weight percent, 5.45 weight percentto 5.50 weight percent, 5.50 weight percent to 5.55 weight percent, 5.55weight percent to 5.60 weight percent, 5.60 weight percent to 5.65weight percent, 5.65 weight percent to 5.70 weight percent, 5.70 weightpercent to 5.75 weight percent, 5.75 weight percent to 5.80 weightpercent, 5.80 weight percent to 5.85 weight percent, 5.85 weight percentto 5.90 weight percent, 5.90 weight percent to 5.95 weight percent, 5.95weight percent to 6.00 weight percent, 6.00 weight percent to 6.05weight percent, 6.05 weight percent to 6.10 weight percent, 6.10 weightpercent to 6.15 weight percent, 6.15 weight percent to 6.20 weightpercent, 6.20 weight percent to 6.25 weight percent, 6.25 weight percentto 6.30 weight percent, 6.30 weight percent to 6.35 weight percent, 6.35weight percent to 6.40 weight percent, 6.40 weight percent to 6.45weight percent, 6.45 weight percent to 6.50 weight percent, 6.50 weightpercent to 6.55 weight percent, 6.55 weight percent to 6.60 weightpercent, 6.60 weight percent to 6.65 weight percent, 6.65 weight percentto 6.70 weight percent, 6.70 weight percent to 6.75 weight percent, 6.75weight percent to 6.80 weight percent, 6.80 weight percent to 6.85weight percent, 6.85 weight percent to 6.90 weight percent, 6.90 weightpercent to 6.95 weight percent, 6.95 weight percent to 7.00 weightpercent, 7.00 weight percent to 7.05 weight percent, 7.05 weight percentto 7.10 weight percent, 7.10 weight percent to 7.15 weight percent, 7.15weight percent to 7.20 weight percent, 7.20 weight percent to 7.25weight percent, 7.25 weight percent to 7.30 weight percent, 7.30 weightpercent to 7.35 weight percent, 7.35 weight percent to 7.40 weightpercent, 7.40 weight percent to 7.45 weight percent, 7.45 weight percentto 7.50 weight percent, 7.50 weight percent to 8.00 weight percent, 8.00weight percent to 8.50 weight percent, 8.50 weight percent to 9.00weight percent, 9.00 weight percent to 9.50 weight percent, 9.50 weightpercent to 10.00 weight percent, 10.00 weight percent to 10.50 weightpercent, 10.50 weight percent to 11.00 weight percent, 11.00 weightpercent to 11.50 weight percent, 11.50 weight percent to 12.00 weightpercent, 12.00 weight percent to 12.50 weight percent, 12.50 weightpercent to 13.00 weight percent, 13.00 weight percent to 13.50 weightpercent, 13.50 weight percent to 14.00 weight percent, 14.00 weightpercent to 14.50 weight percent, 14.50 weight percent to 15.00 weightpercent, 15.00 weight percent to 15.50 weight percent, 15.50 weightpercent to 16.00 weight percent, 16.00 weight percent to 16.50 weightpercent, 16.50 weight percent to 17.00 weight percent, 17.00 weightpercent to 17.50 weight percent, 17.50 weight percent to 18.00 weightpercent, 18.00 weight percent to 18.50 weight percent, 18.50 weightpercent to 19.00 weight percent, 19.00 weight percent to 19.50 weightpercent, 19.50 weight percent to 20.00 weight percent, 20.00 weightpercent to 20.50 weight percent, 20.50 weight percent to 21.00 weightpercent, 21.00 weight percent to 21.50 weight percent, 21.50 weightpercent to 22.00 weight percent, and 22.00 weight percent to 22.50weight percent.

In embodiments, polyphyletic fungi includes psilocybin mushrooms. Inembodiments, the psilocybin mushrooms includes one or more types ofpsilocybin mushrooms selected from the group consisting of: Psilocybeacutipilea, Psilocybe allenii, Psilocybe angustipleurocystidiata,Psilocybe antioquiensis, Psilocybe atlantis, Psilocybe aquamarina,Psilocybe armandii, Psilocybe aucklandii, Psilocybe atlantis, Psilocybeaztecorum, Psilocybe azurescens, Psilocybe baeocystis, Psilocybebanderillensis, Psilocybe bispora, Psilocybe bohemica, Psilocybebrasiliensis, Psilocybe brunneocystidiata, Psilocybe cubensis, Psilocybecaeruleoannulata, Psilocybe caerulescens, Psilocybe caerulipes,Psilocybe callosa, Psilocybe carbonaria, Psilocybe caribaea, Psilocybechuxiongensis, Psilocybe collybioides, Psilocybe columbiana, Psilocybecordispora, Psilocybe cubensis, Psilocybe cyanescens, Psilocybecyanofibrillosa, Psilocybe dumontii, Psilocybe egonii, Psilocybefagicola, Psilocybe farinacea, Psilocybe fimetaria, Psilocybefuliginosa, Psilocybe furtadoana, Psilocybe galindoi, Psilocybegallaeciae, Psilocybe graveolens, Psilocybe guatapensis, Psilocybeguilartensis, Psilocybe heimii, Psilocybe heliconiae, Psilocybeherrerae, Psilocybe hispanica, Psilocybe hoogshagenii, Psilocybeinconspicua, Psilocybe indica, Psilocybe DANLEO, Psilocybe isabelae,Psilocybe jacobsii, Psilocybe jaliscana, Psilocybe kumaenorum, Psilocybelaurae, Psilocybe lazoi, Psilocybe liniformans, Psilocybe mexicana,Psilocybe mairei, Psilocybe makarorae, Psilocybe mammillata, Psilocybemedullosa, Psilocybe meridensis, Psilocybe meridionalis, Psilocybemescaleroensis, Psilocybe moseri, Psilocybe muliercula, Psilocybenaematoliformis, Psilocybe natalensis, Psilocybe natarajanii, Psilocybeneorhombispora, Psilocybe neoxalapensis, Psilocybe ovoideocystidiata,Psilocybe papuana, Psilocybe paulensis, Psilocybe pelliculosa, Psilocybepintonii, Psilocybe pleurocystidiosa, Psilocybe plutonia, Psilocybeportoricensis, Psilocybe pseudoaztecorum, Psilocybe puberula, Psilocybequebecensis, Psilocybe rickii, Psilocybe rostrata, Psilocybe rzedowskii,Psilocybe samuiensis, Psilocybe sativa, Psilocybe schultesii, Psilocybesemilanceata, Psilocybe septentrionalis, Psilocybe serbica, Psilocybesierrae, Psilocybe silvatica, Psilocybe singeri, Psilocybe squamosa,Psilocybe strictipes, Psilocybe stuntzii, Psilocybe subacutipilea,Psilocybe subaeruginascens, Psilocybe subaeruginosa, Psilocybesubbrunneocystidiata, Psilocybe subcaerulipes, Psilocybe subcubensis,Psilocybe subpsilocybioides, Psilocybe subtropicalis, Psilocybetampanensis, Psilocybe thaicordispora, Psilocybe thaiaerugineomaculans,Psilocybe thaiduplicatocystidiata, Psilocybe uruguayensis, Psilocybeuxpanapensis, Psilocybe venenata, Psilocybe villarrealiae, Psilocybeweraroa, Psilocybe wassoniorum, Psilocybe weilii, Psilocybe weldenii,Psilocybe weraroa, Psilocybe wrightii, Psilocybe xalapensis, Psilocybeyungensis, Psilocybe zapotecorum, Psilocybe zapotecoantillarum,Psilocybe zapotecocaribaea, and Psilocybe zapotecorum.

In embodiments, the psilocybin mushrooms are processed to produce analimentary composition including two or more types of psilocybinmushrooms selected from the group consisting of: Psilocybe acutipilea,Psilocybe allenii, Psilocybe angustipleurocystidiata, Psilocybeantioquiensis, Psilocybe atlantis, Psilocybe aquamarina, Psilocybearmandii, Psilocybe aucklandii, Psilocybe atlantis, Psilocybe aztecorum,Psilocybe azurescens, Psilocybe baeocystis, Psilocybe banderillensis,Psilocybe bispora, Psilocybe bohemica, Psilocybe brasiliensis, Psilocybebrunneocystidiata, Psilocybe cubensis, Psilocybe caeruleoannulata,Psilocybe caerulescens, Psilocybe caerulipes, Psilocybe callosa,Psilocybe carbonaria, Psilocybe caribaea, Psilocybe chuxiongensis,Psilocybe collybioides, Psilocybe columbiana, Psilocybe cordispora,Psilocybe cubensis, Psilocybe cyanescens, Psilocybe cyanofibrillosa,Psilocybe dumontii, Psilocybe egonii, Psilocybe fagicola, Psilocybefarinacea, Psilocybe fimetaria, Psilocybe fuliginosa, Psilocybefurtadoana, Psilocybe galindoi, Psilocybe gallaeciae, Psilocybegraveolens, Psilocybe guatapensis, Psilocybe guilartensis, Psilocybeheimii, Psilocybe heliconiae, Psilocybe herrerae, Psilocybe hispanica,Psilocybe hoogshagenii, Psilocybe inconspicua, Psilocybe indica,Psilocybe DANLEO, Psilocybe isabelae, Psilocybe jacobsii, Psilocybejaliscana, Psilocybe kumaenorum, Psilocybe laurae, Psilocybe lazoi,Psilocybe liniformans, Psilocybe mexicana, Psilocybe mairei, Psilocybemakarorae, Psilocybe mammillata, Psilocybe medullosa, Psilocybemeridensis, Psilocybe meridionalis, Psilocybe mescaleroensis, Psilocybemoseri, Psilocybe muliercula, Psilocybe naematoliformis, Psilocybenatalensis, Psilocybe natarajanii, Psilocybe neorhombispora, Psilocybeneoxalapensis, Psilocybe ovoideocystidiata, Psilocybe papuana, Psilocybepaulensis, Psilocybe pelliculosa, Psilocybe pintonii, Psilocybepleurocystidiosa, Psilocybe plutonia, Psilocybe portoricensis, Psilocybepseudoaztecorum, Psilocybe puberula, Psilocybe quebecensis, Psilocyberickii, Psilocybe rostrata, Psilocybe rzedowskii, Psilocybe samuiensis,Psilocybe sativa, Psilocybe schultesii, Psilocybe semilanceata,Psilocybe septentrionalis, Psilocybe serbica, Psilocybe sierrae,Psilocybe silvatica, Psilocybe singeri, Psilocybe squamosa, Psilocybestrictipes, Psilocybe stuntzii, Psilocybe subacutipilea, Psilocybesubaeruginascens, Psilocybe subaeruginosa, Psilocybesubbrunneocystidiata, Psilocybe subcaerulipes, Psilocybe subcubensis,Psilocybe subpsilocybioides, Psilocybe subtropicalis, Psilocybetampanensis, Psilocybe thaicordispora, Psilocybe thaiaerugineomaculans,Psilocybe thaiduplicatocystidiata, Psilocybe uruguayensis, Psilocybeuxpanapensis, Psilocybe venenata, Psilocybe villarrealiae, Psilocybeweraroa, Psilocybe wassoniorum, Psilocybe weilii, Psilocybe weldenii,Psilocybe weraroa, Psilocybe wrightii, Psilocybe xalapensis, Psilocybeyungensis, Psilocybe zapotecorum, Psilocybe zapotecoantillarum,Psilocybe zapotecocaribaea, and Psilocybe zapotecorum. In embodiments,the alimentary composition may include a composition including two ormore types of psilocybin mushrooms.

In embodiments, the alimentary composition may include a compositioninclude cloned spores from two or more types of psilocybin mushroomsselected from the group consisting of: Psilocybe acutipilea, Psilocybeallenii, Psilocybe angustipleurocystidiata, Psilocybe antioquiensis,Psilocybe atlantis, Psilocybe aquamarina, Psilocybe armandii, Psilocybeaucklandii, Psilocybe atlantis, Psilocybe aztecorum, Psilocybeazurescens, Psilocybe baeocystis, Psilocybe banderillensis, Psilocybebispora, Psilocybe bohemica, Psilocybe brasiliensis, Psilocybebrunneocystidiata, Psilocybe cubensis, Psilocybe caeruleoannulata,Psilocybe caerulescens, Psilocybe caerulipes, Psilocybe callosa,Psilocybe carbonaria, Psilocybe caribaea, Psilocybe chuxiongensis,Psilocybe collybioides, Psilocybe columbiana, Psilocybe cordispora,Psilocybe cubensis, Psilocybe cyanescens, Psilocybe cyanofibrillosa,Psilocybe dumontii, Psilocybe egonii, Psilocybe fagicola, Psilocybefarinacea, Psilocybe fimetaria, Psilocybe fuliginosa, Psilocybefurtadoana, Psilocybe galindoi, Psilocybe gallaeciae, Psilocybegraveolens, Psilocybe guatapensis, Psilocybe guilartensis, Psilocybeheimii, Psilocybe heliconiae, Psilocybe herrerae, Psilocybe hispanica,Psilocybe hoogshagenii, Psilocybe inconspicua, Psilocybe indica,Psilocybe DANLEO, Psilocybe isabelae, Psilocybe jacobsii, Psilocybejaliscana, Psilocybe kumaenorum, Psilocybe laurae, Psilocybe lazoi,Psilocybe liniformans, Psilocybe mexicana, Psilocybe mairei, Psilocybemakarorae, Psilocybe mammillata, Psilocybe medullosa, Psilocybemeridensis, Psilocybe meridionalis, Psilocybe mescaleroensis, Psilocybemoseri, Psilocybe muliercula, Psilocybe naematoliformis, Psilocybenatalensis, Psilocybe natarajanii, Psilocybe neorhombispora, Psilocybeneoxalapensis, Psilocybe ovoideocystidiata, Psilocybe papuana, Psilocybepaulensis, Psilocybe pelliculosa, Psilocybe pintonii, Psilocybepleurocystidiosa, Psilocybe plutonia, Psilocybe portoricensis, Psilocybepseudoaztecorum, Psilocybe puberula, Psilocybe quebecensis, Psilocyberickii, Psilocybe rostrata, Psilocybe rzedowskii, Psilocybe samuiensis,Psilocybe sativa, Psilocybe schultesii, Psilocybe semilanceata,Psilocybe septentrionalis, Psilocybe serbica, Psilocybe sierrae,Psilocybe silvatica, Psilocybe singeri, Psilocybe squamosa, Psilocybestrictipes, Psilocybe stuntzii, Psilocybe subacutipilea, Psilocybesubaeruginascens, Psilocybe subaeruginosa, Psilocybesubbrunneocystidiata, Psilocybe subcaerulipes, Psilocybe subcubensis,Psilocybe subpsilocybioides, Psilocybe subtropicalis, Psilocybetampanensis, Psilocybe thaicordispora, Psilocybe thaiaerugineomaculans,Psilocybe thaiduplicatocystidiata, Psilocybe uruguayensis, Psilocybeuxpanapensis, Psilocybe venenata, Psilocybe villarrealiae, Psilocybeweraroa, Psilocybe wassoniorum, Psilocybe weilii, Psilocybe weldenii,Psilocybe weraroa, Psilocybe wrightii, Psilocybe xalapensis, Psilocybeyungensis, Psilocybe zapotecorum, Psilocybe zapotecoantillarum,Psilocybe zapotecocaribaea, and Psilocybe zapotecorum.

In embodiments, the alimentary composition may include a composition ofground psilocybin mushrooms to have a bulk density ranging from one ormore bulk densities ranging from the group consisting of 8 pounds percubic foot to 10 pounds per cubic foot, 10 pounds per cubic foot to 12pounds per cubic foot, 12 pounds per cubic foot to 14 pounds per cubicfoot, 14 pounds per cubic foot to 16 pounds per cubic foot, 16 poundsper cubic foot to 18 pounds per cubic foot, 18 pounds per cubic foot to20 pounds per cubic foot, 20 pounds per cubic foot to 22 pounds percubic foot, 22 pounds per cubic foot to 24 pounds per cubic foot, 24pounds per cubic foot to 26 pounds per cubic foot, 26 pounds per cubicfoot to 28 pounds per cubic foot, 28 pounds per cubic foot to 30 poundsper cubic foot, 30 pounds per cubic foot to 32 pounds per cubic foot, 32pounds per cubic foot to 34 pounds per cubic foot, 34 pounds per cubicfoot to 36 pounds per cubic foot, 36 pounds per cubic foot to 38 poundsper cubic foot, 38 pounds per cubic foot to 40 pounds per cubic foot, 40pounds per cubic foot to 42 pounds per cubic foot, 42 pounds per cubicfoot to 44 pounds per cubic foot, 44 pounds per cubic foot to 46 poundsper cubic foot, 46 pounds per cubic foot to 48 pounds per cubic foot, 48pounds per cubic foot to 50 pounds per cubic foot, 50 pounds per cubicfoot to 52 pounds per cubic foot, 52 pounds per cubic foot to 54 poundsper cubic foot, 54 pounds per cubic foot to 56 pounds per cubic foot, 56pounds per cubic foot to 58 pounds per cubic foot, 58 pounds per cubicfoot to 60 pounds per cubic foot, 60 pounds per cubic foot to 62 poundsper cubic foot, 62 pounds per cubic foot to 64 pounds per cubic foot, 64pounds per cubic foot to 66 pounds per cubic foot, 66 pounds per cubicfoot to 68 pounds per cubic foot, 68 pounds per cubic foot to 70 poundsper cubic foot, 70 pounds per cubic foot to 72 pounds per cubic foot, 72pounds per cubic foot to 74 pounds per cubic foot, 74 pounds per cubicfoot to 76 pounds per cubic foot, 76 pounds per cubic foot to 78 poundsper cubic foot, 78 pounds per cubic foot to 80 pounds per cubic foot, 80pounds per cubic foot to 85 pounds per cubic foot, 85 pounds per cubicfoot to 90 pounds per cubic foot, 90 pounds per cubic foot to 100 poundsper cubic foot.

In embodiments, the alimentary composition may include a cannabinoid. Inembodiments, the alimentary composition may include terpenes. Inembodiments, the alimentary composition may include treated water.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes:

a water content of undried psilocybin mushrooms and/or the undriedalimentary composition having a weight percent ranging from: 80 to 82,82 to 84, 84 to 86, 86 to 88, 88 to 90, 90 to 92, 92 to 94, 94 to 96, or96 to 98;

a water content of dried mushroom having a weight percent ranging from:0.50 to 1.00, 1.00 to 1.50, 1.50 to 2.00, 2.00 to 2.50, 2.50 to 3.00,3.00 to 3.50, 3.50 to 4.00, 4.00 to 4.50, 4.50 to 5.00, 5.00 to 5.50,5.50 to 6.00, 6.00 to 6.50, 6.50 to 7.00, 7.00 to 7.50, 7.50 to 8.00,8.00 to 8.50, 8.50 to 9.00, 9.00 to 9.50, 9.50 to 10.00, 10.00 to 10.50,10.50 to 11.00, 11.00 to 11.50, 11.50 to 12.00, 12.00 to 12.50, 12.50 to13.00, 13.00 to 13.50, 13.50 to 14.00, 14.00 to 14.50, 14.50 to 15.00,15.00 to 15.50, 15.50 to 16.00, 16.00 to 16.50, 16.50 to 17.00, 17.00 to17.50, 17.50 to 18.00, 19.00 to 20.00, or 20.00 to 25.00;

a water activity (Aw) of dried mushrooms ranging from between: 0.05 to0.1, 0.1 to 0.15, 0.15 to 0.2, 0.2 to 0.25, 0.25 to 0.3, 0.3 to 0.35,0.35 to 0.4, 0.4 to 0.45, 0.45 to 0.5, 0.5 to 0.55, or 0.55 to 0.6;

a potassium content on a dry basis ranging from: 3 part per million(ppm) to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to8 ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a calcium content on a dry basis ranging from: 3 part per million (ppm)to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a phosphorous content on a dry basis ranging from: 3 part per million(ppm) to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to8 ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a magnesium content on a dry basis ranging from: 3 part per million(ppm) to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to8 ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a zinc content on a dry basis ranging from: 3 part per million (ppm) to4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8 ppm, 8ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20 ppm, 20ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40 ppm, 40ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60 ppm, 60ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80 ppm, 80ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100 ppm,100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppm to200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm, 275ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to 375ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450 ppmto 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550 ppm,550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppm to650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm, 725ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to 825ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900 ppmto 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

an iron content on a dry basis ranging from: 3 part per million (ppm) to4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8 ppm, 8ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20 ppm, 20ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40 ppm, 40ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60 ppm, 60ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80 ppm, 80ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100 ppm,100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppm to200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm, 275ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to 375ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450 ppmto 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550 ppm,550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppm to650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm, 725ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to 825ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900 ppmto 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a sodium content on a dry basis ranging from: 3 part per million (ppm)to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a manganese content on a dry basis ranging from: 3 part per million(ppm) to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to8 ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm;

a copper content on a dry basis ranging from: 3 part per million (ppm)to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm; and

a selenium content on a dry basis ranging from: 3 part per million (ppm)to 4 ppm, 4 ppm to 5 ppm, 5 ppm to 6 ppm, 6 ppm to 7 ppm, 7 ppm to 8ppm, 8 ppm to 9 ppm, 9 ppm to 10 ppm, 10 ppm to 15 ppm, 15 ppm to 20ppm, 20 ppm to 25 ppm, 25 ppm to 30 ppm, 30 ppm to 35 ppm, 35 ppm to 40ppm, 40 ppm to 45 ppm, 45 ppm to 50 ppm, 50 ppm to 55 ppm, 55 ppm to 60ppm, 60 ppm to 65 ppm, 65 ppm to 70 ppm, 70 ppm to 75 ppm, 75 ppm to 80ppm, 80 ppm to 85 ppm, 85 ppm to 90 ppm, 90 ppm to 95 ppm, 95 ppm to 100ppm, 100 ppm to 125 ppm, 125 ppm to 150 ppm, 150 ppm to 175 ppm, 175 ppmto 200 ppm, 200 ppm to 225 ppm, 225 ppm to 250 ppm, 250 ppm to 275 ppm,275 ppm to 300 ppm, 300 ppm to 325 ppm, 325 ppm to 350 ppm, 350 ppm to375 ppm, 375 ppm to 400 ppm, 400 ppm to 425 ppm, 425 ppm to 450 ppm, 450ppm to 475 ppm, 475 ppm to 500 ppm, 500 ppm to 525 ppm, 525 ppm to 550ppm, 550 ppm to 575 ppm, 575 ppm to 600 ppm, 600 ppm to 625 ppm, 625 ppmto 650 ppm, 650 ppm to 675 ppm, 675 ppm to 700 ppm, 700 ppm to 725 ppm,725 ppm to 750 ppm, 750 ppm to 775 ppm, 775 ppm to 800 ppm, 800 ppm to825 ppm, 825 ppm to 850 ppm, 850 ppm to 875 ppm, 875 ppm to 900 ppm, 900ppm to 1000 ppm, 1000 ppm to 1100 ppm, 1100 ppm to 1200 ppm, 1200 ppm to1300 ppm, 1300 ppm to 1400 ppm, 1400 ppm to 1500 ppm, 1500 ppm to 2000ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm,3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm, or 4500 ppm to 5000 ppm.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes:

a water content of undried psilocybin mushrooms and/or the undriedalimentary composition having a weight percent ranging from: 80 to 82,82 to 84, 84 to 86, 86 to 88, 88 to 90, 90 to 92, 92 to 94, 94 to 96, or96 to 98;

a protein content of undried psilocybin mushrooms and/or the undriedalimentary composition having a weight percent ranging from: 0.25 to0.75, 0.75 to 1.25, 1.25 to 1.75, 1.75 to 2.25, 2.25 to 2.75, 2.75 to3.25, 3.25 to 3.75, 3.75 to 4.25, 4.25 to 4.75, 4.75 to 5.25, 5.25 to5.75, 5.75 to 6.25, 6.25 to 6.75, 6.75 to 7.25, 7.25 to 7.75, 7.75 to8.25, 8.25 to 8.75, 8.75 to 9.25, 9.25 to 9.75, 9.75 to 10.00, 10.00 to10.25, 10.25 to 10.75, 10.75 to 11.25, 11.25 to 11.75, 11.75 to 12.25,12.25 to 12.75, 12.75 to 13.25, 13.25 to 13.75, or 13.75 to 14.25;

a carbohydrate content of undried psilocybin mushrooms and/or theundried alimentary composition having a weight percent ranging from:0.25 to 0.75, 0.75 to 1.25, 1.25 to 1.75, 1.75 to 2.25, 2.25 to 2.75,2.75 to 3.25, 3.25 to 3.75, 3.75 to 4.25, 4.25 to 4.75, 4.75 to 5.25,5.25 to 5.75, 5.75 to 6.25, 6.25 to 6.75, 6.75 to 7.25, 7.25 to 7.75,7.75 to 8.25, 8.25 to 8.75, 8.75 to 9.25, 9.25 to 9.75, 9.75 to 10.00,10.00 to 10.25, 10.25 to 10.75, 10.75 to 11.25, 11.25 to 11.75, 11.75 to12.25, 12.25 to 12.75, 12.75 to 13.25, 13.25 to 13.75, or 13.75 to14.25;

an ash content of undried psilocybin mushrooms and/or the undriedalimentary composition having a weight percent ranging from: 0.25 to0.75, 0.75 to 1.25, 1.25 to 1.75, 1.75 to 2.25, 2.25 to 2.75, 2.75 to3.25, 3.25 to 3.75, 3.75 to 4.25, 4.25 to 4.75, 4.75 to 5.25, 5.25 to5.75, 5.75 to 6.25, 6.25 to 6.75, 6.75 to 7.25, 7.25 to 7.75, 7.75 to8.25, 8.25 to 8.75, 8.75 to 9.25, 9.25 to 9.75, 9.75 to 10.00, 10.00 to10.25, 10.25 to 10.75, 10.75 to 11.25, 11.25 to 11.75, 11.75 to 12.25,12.25 to 12.75, 12.75 to 13.25, 13.25 to 13.75, or 13.75 to 14.25;and/or

a fat content of undried psilocybin mushrooms and/or the undriedalimentary composition having a weight percent ranging from: 0.25 to0.75, 0.75 to 1.25, 1.25 to 1.75, 1.75 to 2.25, 2.25 to 2.75, 2.75 to3.25, 3.25 to 3.75, 3.75 to 4.25, 4.25 to 4.75, 4.75 to 5.25, 5.25 to5.75, 5.75 to 6.25, 6.25 to 6.75, 6.75 to 7.25, 7.25 to 7.75, 7.75 to8.25, 8.25 to 8.75, 8.75 to 9.25, 9.25 to 9.75, 9.75 to 10.00, 10.00 to10.25, 10.25 to 10.75, 10.75 to 11.25, 11.25 to 11.75, 11.75 to 12.25,12.25 to 12.75, 12.75 to 13.25, 13.25 to 13.75, or 13.75 to 14.25.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition include: a water activity (Aw) ranging from between: 0.800to 0.805, 0.805 to 0.810, 0.810 to 0.815, 0.815 to 0.820, 0.820 to0.825, 0.825 to 0.830, 0.830 to 0.835, 0.835 to 0.840, 0.840 to 0.845,0.845 to 0.850, 0.850 to 0.855, 0.855 to 0.860, 0.860 to 0.865, 0.865 to0.870, 0.870 to 0.875, 0.875 to 0.880, 0.880 to 0.885, 0.885 to 0.890,0.890 to 0.895, 0.895 to 0.900, 0.900 to 0.905, 0.905 to 0.910, 0.910 to0.915, 0.915 to 0.920, 0.920 to 0.925, 0.925 to 0.930, 0.930 to 0.935,0.935 to 0.940, 0.940 to 0.945, 0.945 to 0.950, 0.950 to 0.955, 0.955 to0.960, 0.960 to 0.965, 0.965 to 0.970, 0.970 to 0.975, 0.975 to 0.980,0.980 to 0.985, 0.985 to 0.990, 0.990 to 0.991, 0.991 to 0.992, 0.992 to0.993, 0.993 to 0.994, 0.994 to 0.995, 0.995 to 0.996, 0.996 to 0.997,0.997 to 0.998, 0.998 to 0.999, 0.9990 to 0.9991, 0.9991 to 0.9992,0.9992 to 0.9993, 0.9993 to 0.9994, 0.9994 to 0.9995, 0.9995 to 0.9996,0.9996 to 0.9997, 0.9997 to 0.9998, or 0.9998 to 0.9999.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes: a carbon content of dried psilocybin mushroomshaving a weight percent on a dry basis ranging from: 15.00 to 17.50,17.50 to 20.00, 20.00 to 22.50, 22.50 to 25.00, 25.00 to 27.50, 27.50 to30.00, 30.00 to 32.50, 32.50 to 35.00, 35.00 to 37.50, 37.50 to 40.00,40.00 to 42.50, 42.50 to 45.00, 45.00 to 47.50, 47.50 to 50.00, 50.00 to52.50, or 52.50 to 55.00. In embodiments, the psilocybin mushroomsand/or the alimentary composition includes: a carbon content of driedpsilocybin mushrooms having a weight percent on a dry basis rangingfrom: 30.00 to 45.00.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes: a hydrogen content of dried psilocybin mushroomshaving a weight percent on a dry basis ranging from: 2 to 3, 3 to 4, 4to 5, 5 to 6, 6 to 7, 7 to 8, 8 to 9, 9 to 10, 10 to 11, 11 to 12, 12 to13, 13 to 14, 14 to 15, 15 to 16, 16 to 17, 17 to 18, 18 to 19, or 19 to20. In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes: a hydrogen content of dried psilocybin mushroomshaving a weight percent on a dry basis ranging from: 4 to 10.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes: a nitrogen content of dried psilocybin mushroomshaving a weight percent on a dry basis ranging from: 0.25 to 1.50, 1.50to 2.75, 2.75 to 4.00, 4.00 to 5.25, 5.25 to 6.50, 6.50 to 7.75, 7.75 to9.00, 9.00 to 10.25, 10.25 to 11.50, 11.50 to 12.75, 12.75 to 14.00, or14.00 to 15.25. In embodiments, the psilocybin mushrooms and/or thealimentary composition includes: a nitrogen content of dried psilocybinmushrooms having a weight percent on a dry basis ranging from: 2.75 to9.00.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition includes: a oxygen content of dried psilocybin mushroomshaving a weight percent on a dry basis ranging from: 15.00 to 17.50,17.50 to 20.00, 20.00 to 22.50, 22.50 to 25.00, 25.00 to 27.50, 27.50 to30.00, 30.00 to 32.50, 32.50 to 35.00, 35.00 to 37.50, 37.50 to 40.00,40.00 to 42.50, 42.50 to 45.00, 45.00 to 47.50, 47.50 to 50.00, 50.00 to52.50, or 52.50 to 55.00.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may be grown within the Insect Production SuperstructureSystem (IPSS). In embodiments, the psilocybin mushrooms and/or thealimentary composition may be processed within the Insect ProductionSuperstructure System (IPSS). In embodiments, the psilocybin mushroomsand/or the alimentary composition may be grown within the farmingsuperstructure system (FSS) using any disclosed systems or methods thatare disclosed to process insects.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may be processed within the farming superstructure system(FSS). In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may be processed within the farming superstructure system(FSS) using any disclosed systems or methods that are used to processcannabis and to extract cannabinoids from cannabis.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may be processed within the farming superstructure system(FSS) using a rotary evaporator, falling film tubular evaporator,rising/falling film tubular evaporator, rising film tubular evaporator,forced circulation evaporator, internal pump forced circulationevaporator, plate evaporator, evaporative cooler, multiple-effectevaporator, thermal vapor recompression evaporator, mechanical vaporrecompression evaporator, flash tank, a crystallizer, a draft tube andbaffle crystallizer, cooling crystallization, evaporativecrystallization, fractional crystallization, a distillation column, or aspray dryer.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may be processed within the farming superstructure system(FSS) using a continuous process for the purification of psilocybin,psilocin, baeocystin, and/or norbaeocystin extracted from psilocybinmushrooms and/or the alimentary composition using continuous simulatedmoving bed processes and micro and nanofiltration without the additionof organic solvents to obtain a purified psilocybin, psilocin,baeocystin, and/or norbaeocystin product. The psilocybin, psilocin,baeocystin, and/or norbaeocystin can be used to create foodstuffs,emulsions, drugs, beverages, alcoholic beverages, non-alcoholicbeverages, energy drinks, softgels, fitness supplements, or formedicinal or recreational uses, and pet food.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may be included in fitness and/or bodybuilding supplementsincluding one or more selected from the group consisting of arginine,beta-alanine, beta-ecdysterone, branched-chain amino acid (BCAA),caffeine, carnitine, casein protein powder, citrulline malate, creatine,energy supplements, fish oil, glutamine, growth hormone supplements,high molecular-weight carbs (vitargo), hormonal supplements, lysine,nitric oxide boosters, ornithine, prohormones, testosterone boosters,whey protein, zma (zinc, magnesium aspartate and vitamin B6), orβ-Hydroxy β-methylbutyric acid (HMB).

In embodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with milk, milkpowder, whole milk powder, goat milk, soy milk, almond milk, coconutmilk, oat milk, rice milk, cashew milk, macadamia milk, whole milk, 2%milk, 1% milk, organic milk, lactose-free milk, half and half, cream,buttermilk, or chocolate milk. In embodiments, the psilocybin mushroomsand/or the alimentary composition may be mixed with milk, milk powder,whole milk powder, goat milk, soy milk, almond milk, coconut milk, oatmilk, rice milk, cashew milk, macadamia milk, whole milk, 2% milk, 1%milk, organic milk, lactose-free milk, half and half, cream, buttermilk,or chocolate milk.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may be included in fitness and/or bodybuilding supplementsincluding one or more selected from the group consisting of arginine,beta-alanine, beta-ecdysterone, branched-chain amino acid (BCAA),caffeine, carnitine, casein protein powder, citrulline malate, creatine,energy supplements, fish oil, glutamine, growth hormone supplements,high molecular-weight carbs (vitargo), hormonal supplements, lysine,nitric oxide boosters, ornithine, prohormones, testosterone boosters,whey protein, zma (zinc, magnesium aspartate and vitamin B6), orβ-Hydroxy β-methylbutyric acid (HMB).

In embodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be included in fitness and/orbodybuilding supplements including one or more selected from the groupconsisting of arginine, beta-alanine, beta-ecdysterone, branched-chainamino acid (BCAA), caffeine, carnitine, casein protein powder,citrulline malate, creatine, energy supplements, fish oil, glutamine,growth hormone supplements, high molecular-weight carbs (vitargo),hormonal supplements, lysine, nitric oxide boosters, ornithine,prohormones, testosterone boosters, whey protein, zma (zinc, magnesiumaspartate and vitamin B6), or β-Hydroxy β-methylbutyric acid (HMB).

In embodiments, the cannabinoids may be included in fitness and/orbodybuilding supplements including one or more selected from the groupconsisting of arginine, beta-alanine, beta-ecdysterone, branched-chainamino acid (BCAA), caffeine, carnitine, casein protein powder,citrulline malate, creatine, energy supplements, fish oil, glutamine,growth hormone supplements, high molecular-weight carbs (vitargo),hormonal supplements, lysine, nitric oxide boosters, ornithine,prohormones, testosterone boosters, whey protein, ZMA (zinc, magnesiumaspartate and vitamin B6), or β-Hydroxy β-methylbutyric acid (HMB).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition may mixed with insect oil. In embodiments, the psilocybin,psilocin, baeocystin, and/or norbaeocystin may be with insect oil. Inembodiments, the cannabinoids may be with insect oil.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may extracted with psilocybin mushrooms and/or thealimentary composition with a solvent includes one or more from thegroup consisting of acetone, alcohol, oil, butane, butter, carbondioxide, coconut oil, ethanol, ether, gas, gaseous carbon dioxide,hexane, insect lipids, isobutane, isopropanol, liquid carbon dioxide,liquid, naphtha, olive oil, pentane, propane, R134 refrigerant gas,subcritical carbon dioxide, supercritical carbon dioxide, and vapor.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may extracted with a solvent including one or moreselected from the group consisting of a cannabinoid, lipids extractedfrom insects, almond oil, animal-based oils, apricot kernel oil, avocadooil, brazil nut oil, butter, canola oil, cashew oil, cocoa butter,coconut oil, cooking oil, coffee oil, corn oil, cottonseed oil, fishoil, grapeseed oil, hazelnut oil, hemp oil, hop oil. insect oil, lard,lard oil, macadamia nut oil, mustard oil, olive oil, palm kernel oil,palm oil, peanut oil, peppermint oil, rapeseed oil, rice oil, rice branoil, safflower oil, semi-refined sesame oil, semi-refined sunflower oil,sesame oil, soybean oil, tallow of beef, tallow of mutton, vegetableoil, and walnut oil.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may extracted with psilocybin mushrooms and/or thealimentary composition with a solvent includes ethanol, the ethanol hasa water concentration selected from the group consisting of 50 to 51, 51to 52, 52 to 53, 53 to 54, 54 to 55, 55 to 56, 56 to 57, 57 to 58, 58 to59, 59 to 60, 60 to 61, 61 to 62, 62 to 63, 63 to 64, 64 to 65, 65 to66, 66 to 67, 67 to 68, 68 to 69, 69 to 70, 70 to 71, 71 to 72, 72 to73, 73 to 74, 74 to 75, 75 to 76, 76 to 77, 77 to 78, 78 to 79, 79 to80, 80 to 81, 81 to 82, 82 to 83, 83 to 84, 84 to 85, 85 to 86, 86 to87, 87 to 88, 88 to 89, 89 to 90, 90 to 91, 91 to 92, 92 to 93, 93 to94, 94 to 95, 95 to 95.25, 95.25 to 95.5, 95.5 to 95.75, 95.75 to 96, 96to 96.25, 96.25 to 96.5, 96.5 to 96.75, 96.75 to 97, 97 to 97.25, 97.25to 97.5, 97.5 to 97.75, 97.75 to 98, 98 to 98.25, 98.25 to 98.5, 98.5 to98.6, 98.6 to 98.7, 98.7 to 98.8, 98.8 to 98.9, 98.9 to 99, 99 to 99.1,99.1 to 99.2, 99.2 to 99.3, 99.3 to 99.4, 99.4 to 99.45, 99.45 to 99.5,99.5 to 99.55, 99.55 to 99.6, 99.6 to 99.65, 99.65 to 99.7, 99.7 to99.75, 99.75 to 99.8, 99.8 to 99.85, 99.85 to 99.9, 99.9 to 99.905,99.905 to 99.91, 99.910 to 99.915, 99.915 to 99.92, 99.920 to 99.925,99.925 to 99.93, 99.930 to 99.935, 99.935 to 99.94, 99.940 to 99.945,99.945 to 99.95, 99.950 to 99.955, 99.955 to 99.96, 99.960 to 99.965,99.965 to 99.97, 99.970 to 99.975, 99.975 to 99.98, 99.980 to 99.985,99.985 to 99.99, 99.990 to 99.991, 99.991 to 99.992, 99.992 to 99.993,99.993 to 99.994, 99.994 to 99.995, 99.995 to 99.996, 99.996 to 99.997,99.997 to 99.998, 99.998 to 99.999, or 99.999 to 100.000.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may extracted from the psilocybin mushrooms and/or thealimentary composition with a solvent for a time duration ranging from 1minute to 2 minutes, 2 minutes to 4 minutes, 4 minutes to 6 minutes, 6minutes to 8 minutes, 8 minutes to 10 minutes, 10 minutes to 12 minutes,12 minutes to 14 minutes, 14 minutes to 16 minutes, 16 minutes to 18minutes, 18 minutes to 20 minutes, 20 minutes to 25 minutes, 25 minutesto 30 minutes, 30 minutes to 35 minutes, 35 minutes to 40 minutes, 40minutes to 45 minutes, 45 minutes to 50 minutes, 50 minutes to 55minutes, 55 minutes to 1 hour, 1 hour to 1.5 hours, 1.5 hours to 2hours, 2 hours to 2.5 hours, 2.5 hours to 3 hours, 3 hours to 3.5 hours,3.5 hours to 4 hours, 4 hours to 4.5 hours, 4.5 hours to 5 hours, 5hours to 5.5 hours, 5.5 hours to 6 hours, 6 hours to 18 hours, 18 hoursto 24 hours, 24 hours to 36 hours, 36 hours to 48 hours, 48 hours to 60hours, 60 hours to 72 hours, 72 hours to 84 hours, or 84 hours to 96hours.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may extracted from the psilocybin mushrooms and/or thealimentary composition with ethanol for a time duration ranging from 1minute to 2 minutes, 2 minutes to 4 minutes, 4 minutes to 6 minutes, 6minutes to 8 minutes, 8 minutes to 10 minutes, 10 minutes to 12 minutes,12 minutes to 14 minutes, 14 minutes to 16 minutes, 16 minutes to 18minutes, 18 minutes to 20 minutes, 20 minutes to 25 minutes, 25 minutesto 30 minutes, 30 minutes to 35 minutes, 35 minutes to 40 minutes, 40minutes to 45 minutes, 45 minutes to 50 minutes, 50 minutes to 55minutes, 55 minutes to 1 hour, 1 hour to 1.5 hours, 1.5 hours to 2hours, 2 hours to 2.5 hours, 2.5 hours to 3 hours, 3 hours to 3.5 hours,3.5 hours to 4 hours, 4 hours to 4.5 hours, 4.5 hours to 5 hours, 5hours to 5.5 hours, 5.5 hours to 6 hours, 6 hours to 18 hours, 18 hoursto 24 hours, 24 hours to 36 hours, 36 hours to 48 hours, 48 hours to 60hours, 60 hours to 72 hours, 72 hours to 84 hours, or 84 hours to 96hours.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may extracted with a solvent includes ethanol, the ethanolhas a reduced water concentration by passing the ethanol past anadsorbent, wherein, the adsorbent is comprised of one or more selectedfrom the group consisting of silica gel, alumina, silica, cellulosepowder, a polymer, polymeric beads, a macroporous adsorption resin, DOWXAD 418, molecular sieves, a polar macroporous adsorption resin,floridin, diatomite, zeolites, a catalyst, a resin, an ion-exchangeresin, ion-exchange polymer, clay, ceramic material, activated carbon, acation-exchange resin, an anion-exchange resin, bentonite, perlite, flyash, chitin, charcoal, a solid substance, magnesia, titanium oxide,glass, fluorinated carbon, silicate, kaolin, a hollow substance, aporous substance.

In embodiments, the psilocybin, psilocin, baeocystin, and/ornorbaeocystin may be extracted to form a psilocybin extract, a psilocinextract, a baeocystin extract, and/or a norbaeocystin extract. Inembodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be a liquid. In embodiments,the psilocybin extract, psilocin extract, baeocystin extract, and/ornorbaeocystin extract is a powder.

In embodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract is a powder may have a particlesize ranging from one or more from the group consisting of 0.001nanometers to 0.1 nanometers, 0.1 nanometers to 0.5 nanometers, 0.5nanometers to 1 nanometer, 1 nanometer to 5 nanometers, 5 nanometers to10 nanometers, 10 nanometers to 15 nanometers, 15 nanometers to 20nanometers, 20 nanometers to 25 nanometers, 25 nanometers to 30nanometers, 30 nanometers to 35 nanometers, 35 nanometers to 40nanometers, 40 nanometers to 45 nanometers, 45 nanometers to 50nanometers, 50 nanometers to 55 nanometers, 55 nanometers to 60nanometers, 60 nanometers to 65 nanometers, 65 nanometers to 70nanometers, 70 nanometers to 75 nanometers, 75 nanometers to 80nanometers, 80 nanometers to 85 nanometers, 85 nanometers to 90nanometers, 90 nanometers to 95 nanometers, 95 nanometers to 100nanometers, 100 nanometers to 200 nanometers, 200 nanometers to 300nanometers, 300 nanometers to 400 nanometers, 400 nanometers to 500nanometers, 500 nanometers to 600 nanometers, 600 nanometers to 700nanometers, 700 nanometers to 800 nanometers, and 800 nanometers to 900nanometers.

In embodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract is a powder may have a particlesize ranging from 50 microns to 60 microns, 60 microns to 70 microns, 70microns to 80 microns, 80 microns to 90 microns, 90 microns to 100microns, 100 microns to 150 microns, 150 microns to 200 microns, 200microns to 250 microns, 250 microns to 300 microns, 300 microns to 350microns, 350 microns to 400 microns, 400 microns to 450 microns, 450microns to 500 microns, 500 microns to 550 microns, 550 microns to 600microns, 600 microns to 650 microns, 650 microns to 700 microns, 700microns to 750 microns, 750 microns to 800 microns, 800 microns to 850microns, 850 microns to 900 microns, 900 microns to 950 microns, and 950microns to 1,000 microns.

In embodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract is a powder may have a particlesize ranging from 1 microns to 5 microns, 5 microns to 10 microns, 10microns to 30 microns, 30 microns to 50 microns, 50 microns to 70microns, 70 microns to 90 microns, 90 microns to 110 microns, 110microns to 130 microns, 130 microns to 150 microns, 150 microns to 170microns, 170 microns to 190 microns, 190 microns to 210 microns, 210microns to 230 microns, and 230 microns to 250 microns.

In embodiments, the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract includes a crystal structureformed by nucleation followed by crystal growth. In embodiments, thepsilocybin extract, psilocin extract, baeocystin extract, and/ornorbaeocystin extract includes a crystal structure including a singlecrystal or monocrystalline solid including a material in which a crystallattice of the entire sample is continuous and unbroken to the edges ofthe sample, with no grain boundaries.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: acidifyingagents (acetic acid, glacial acetic acid, citric acid, fumaric acid,hydrochloric acid, diluted hydrochloric acid, malic acid, nitric acid,phosphoric acid, diluted phosphoric acid, sulfuric acid, tartaric acid).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: alkalizingagents (ammonia solution, ammonium carbonate, diethanolamine,diisopropanolamine, potassium hydroxide, sodium bicarbonate, sodiumborate, sodium carbonate, sodium hydroxide, trolamine).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: antifoamingagents (dimethicone, simethicone).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: antimicrobialpreservatives (benzalkonium chloride, benzalkonium chloride solution,benzethonium chloride, benzoic acid, benzyl alcohol, butylparaben,cetylpyridinium chloride, chlorobutanol, chlorocresol, cresol,dehydroacetic acid, ethylparaben, methylparaben, methylparaben sodium,phenol, phenylethyl alcohol, phenylmercuric acetate, phenylmercuricnitrate, potassium benzoate, potassium sorbate, propylparaben,propylparaben sodium, sodium benzoate, sodium dehydroacetate, sodiumpropionate, sorbic acid, thimerosal, thymol).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: antioxidants(ascorbic acid, ascorbyl palmitate, butylated hydroxyanisole, butylatedhydroxytoluene, hypophosphorous acid, monothioglycerol, propyl gallate,sodium formaldehyde sulfoxylate, sodium metabisulfite, sodiumthiosulfate, sulfur dioxide, tocopherol, tocopherols excipient).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: bufferingagents (acetic acid, ammonium carbonate, ammonium phosphate, boric acid,citric acid, lactic acid, phosphoric acid, potassium citrate, potassiummetaphosphate, potassium phosphate monobasic, sodium acetate, sodiumcitrate, sodium lactate solution, dibasic sodium phosphate, monobasicsodium phosphate).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: chelatingagents (edetate disodium, ethylenediaminetetraacetic acid and salts,edetic acid).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: coating agents(sodium carboxymethylcellulose, cellulose acetate, cellulose acetatephthalate, ethylcellulose, gelatin, vegetarian gelatin substitutes,vegan gelatin substitutes, pharmaceutical glaze, hydroxypropylcellulose, hydroxypropyl methylcellulose, hydroxypropyl methylcellulosephthalate, methacrylic acid copolymer, methylcellulose, polyvinylacetate phthalate, shellac, sucrose, titanium dioxide, carnauba wax,microcrystalline wax, zein); Colorants (caramel, red, yellow, black orblends, ferric oxide).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: complexingagents (ethylenediaminetetraacetic acid and salts (EDTA), edetic acid,gentisic acid ethanolamide, oxyquinoline sulfate); Desiccants (calciumchloride, calcium sulfate, silicon dioxide).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: emulsifyingand/or solubilizing agents (acacia, cholesterol, diethanolamine(adjunct), glyceryl monostearate, lanolin alcohols, mono- anddi-glycerides, monoethanolamine (adjunct), lecithin, oleic acid(adjunct), oleyl alcohol (stabilizer), poloxamer, polyoxyethylene 50stearate, polyoxyl 35 castor oil, polyoxyl 40 hydrogenated castor oil,polyoxyl 10 oleyl ether, polyoxyl 20 cetostearyl ether, polyoxyl 40stearate, polysorbate 20, polysorbate 40, polysorbate 60, polysorbate80, diacetate, monostearate, sodium lauryl sulfate, sodium stearate,sorbitan monolaurate, sorbitan monooleate, sorbitan monopalmitate,sorbitan monostearate, stearic acid, trolamine, emulsifying wax).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: filtering aids(powdered cellulose, purified siliceous earth); Flavors and perfumes(anethole, benzaldehyde, ethyl vanillin, menthol, methyl salicylate,monosodium glutamate, orange flower oil, peppermint, peppermint oil,peppermint spirit, rose oil, stronger rose water, thymol, tolu balsamtincture, vanilla, vanilla tincture, vanillin).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: humectants(glycerol, hexylene glycol, sorbitol).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: plasticizers(e.g., castor oil, diacetylated monoglycerides, diethyl phthalate,glycerol, mono- and di-acetylated monoglycerides, propylene glycol,triacetin, triethyl citrate).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: polymers (e.g.,cellulose acetate, alkyl celluloses, hydroxyalkyl, acrylic polymers andcopolymers).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: solvents(acetone, alcohol, diluted alcohol, amylene hydrate, benzyl benzoate,butyl alcohol, carbon tetrachloride, chloroform, corn oil, cottonseedoil, ethyl acetate, glycerol, hexylene glycol, isopropyl alcohol, methylalcohol, methylene chloride, methyl isobutyl ketone, mineral oil, peanutoil, propylene carbonate, sesame oil, treated water).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: sorbents(powdered cellulose, charcoal, purified siliceous earth).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: carbon dioxidesorbents (barium hydroxide lime, soda lime).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: stiffeningagents (hydrogenated castor oil, cetostearyl alcohol, cetyl alcohol,cetyl esters wax, hard fat, paraffin, polyethylene excipient, stearylalcohol, emulsifying wax, white wax, yellow wax).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: suspendingand/or viscosity-increasing agents (acacia, agar, alginic acid, aluminummonostearate, bentonite, purified bentonite, magma bentonite, carbomer,carboxymethylcellulose calcium, carboxymethylcellulose sodium,carboxymethylcellulose sodium 12, carrageenan, microcrystalline andcarboxymethylcellulose sodium cellulose, dextrin, gelatin, vegetariangelatin substitutes, vegan gelatin substitutes, guar gum, hydroxyethylcellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose,magnesium aluminum silicate, methylcellulose, pectin, polyethyleneoxide, polyvinyl alcohol, povidone, alginate, silicon dioxide, colloidalsilicon dioxide, sodium alginate, tragacanth, xanthan gum).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: sweeteningagents (aspartame, dextrates, dextrose, excipient dextrose, fructose,mannitol, saccharin, calcium saccharin, sodium saccharin, sorbitol,solution sorbitol, sucrose, compressible sugar, confectioner's sugar,syrup).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: surfactants(simethicone).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: tablet binders(acacia, alginic acid, sodium carboxymethylcellulose, microcrystallinecellulose, dextrin, ethylcellulose, gelatin, vegetarian gelatinsubstitutes, vegan gelatin substitutes, liquid glucose, guar gum,hydroxypropyl methylcellulose, methylcellulose, polyethylene oxide,povidone, pregelatinized starch, syrup).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: tablet and/orcapsule diluents (calcium carbonate, dibasic calcium phosphate, tribasiccalcium phosphate, calcium sulfate, microcrystalline cellulose, powderedcellulose, dextrates, dextrin, dextrose excipient, fructose, kaolin,lactose, mannitol, sorbitol, starch, pregelatinized starch, sucrose,compressible sugar, confectioner's sugar).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: tabletdisintegrants (alginic acid, microcrystalline cellulose, croscarmellosesodium, crospovidone, polacrilin potassium, sodium starch glycolate,starch, pregelatinized starch).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: tablet and/orcapsule lubricants (calcium stearate, glyceryl behenate, magnesiumstearate, light mineral oil, sodium stearyl fumarate, stearic acid,purified stearic acid, talc, hydrogenated vegetable oil, zinc stearate).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: thickeningagents (gelatin having a Bloom strength of 50-100, an animal-freegelatin, a vegan gelatin, agar, agar-agar, kanten, carrageenan,carrageen, or irish moss vegan jel (vegetable gum adipic acid, tapiocadextrin, calcium phosphate, and potassium citrate)).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: tonicity agent(dextrose, glycerol, mannitol, potassium chloride, sodium chloride).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: a flavoringand/or sweetener (aromatic elixir, compound benzaldehyde elixir,iso-alcoholic elixir, peppermint water, sorbitol solution, syrup, tolubalsam syrup).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: an oleaginouscompound (almond oil, corn oil, cottonseed oil, ethyl oleate, isopropylmyristate, isopropyl palmitate, mineral oil, light mineral oil, myristylalcohol, octyl dodecanol, olive oil, peanut oil, persic oil, sesame oil,soybean oil, squalane).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: a sterilecompound (Bacteriostatic water for injection, bacteriostatic sodiumchloride injection)

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with:viscosity-increasing agents (suspending agents, agar agar, calciumalginate, curdlan, gelatin, gellan gum, glycerol esters of wood rosin,hydroxypropyl methyl cellulose, jelly powder, konjac gum,microcrystalline cellulose (MCC), pectin, propylene glycol alginate(PGA) semi-refined carrageenan, sodium alginate, sodium carboxymethylcellulose, tamarind gum polysaccharide, tara gum, xanthan gum).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: water repellingagents (cyclomethicone, dimethicone, simethicone).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: a solubilizingagent (benzalkonium chloride, benzethonium chloride, cetylpyridiniumchloride, docusate sodium, nonoxynol 9, nonoxynol 10, octoxynol 9,poloxamer, polyoxyl 35 castor oil, polyoxyl 40, hydrogenated castor oil,polyoxyl 50 stearate, polyoxyl 10 oleyl ether, polyoxyl 20, cetostearylether, polyoxyl 40 stearate, polysorbate 20, polysorbate 40, polysorbate60, polysorbate 80, sodium lauryl sulfate, sorbitan monolaurate,sorbitan monooleate, sorbitan monopalmitate, sorbitan monostearate,tyloxapol).

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with: one or morewaxes selected from the group consisting of acacia decurrens flower cera(mimosa flower wax), almond wax, avocado wax, beery wax, bees wax,cananga odorata flower cera (ylang ylang flower wax), candelilla wax,Cannabis sativa oil, castor wax, cupuacu butter, floral wax, hemp wax,hydrogenated almond oil, hydrogenated animal-based oils, hydrogenatedapricot kernel oil, hydrogenated avocado oil, hydrogenated brazil nutoil, hydrogenated canola oil, hydrogenated cashew oil, hydrogenatedcocoa butter, hydrogenated coconut oil, hydrogenated coffee oil,hydrogenated corn oil, hydrogenated cottonseed oil, hydrogenatedgrapeseed oil, hydrogenated hazelnut oil, hydrogenated hemp oil,hydrogenated hop oil, hydrogenated insect oil, hydrogenated lard oil,hydrogenated lard, hydrogenated macadamia nut oil, hydrogenated mustardoil, hydrogenated olive oil, hydrogenated palm kernel oil, hydrogenatedpalm oil, hydrogenated peanut oil, hydrogenated peppermint oil,hydrogenated rapeseed oil, hydrogenated rice bran oil, hydrogenated riceoil, hydrogenated safflower oil, hydrogenated semi-refined sesame oil,hydrogenated semi-refined sunflower oil, hydrogenated sesame oil,hydrogenated soybean oil, hydrogenated walnut oil, jasminum grandiflorumflower cera (jasmine flower wax), Lavandula angustifolia flower cera(lavender flower wax), mmyrica fruit wax, olive wax, prunus amygdalusdulcis oil, rapeseed wax, rice bran wax, rosa damascene flower cera(rose flower wax), shea butter, soybean wax, sunflower wax, vegan wax,vegetable wax, wax from Mexican shrub Euphorbia antisyphilitica, and waxfrom the berries of rhus verniciflua.

In embodiments, the psilocybin mushrooms and/or the alimentarycomposition and/or the psilocybin extract, psilocin extract, baeocystinextract, and/or norbaeocystin extract may be mixed with esterifiedinsect lipids.

In embodiments, the psilocybin extract includes a molecular weightranging from 284.252 pounds per pound-mole and a melting point rangingfrom 428 to 442 degrees Fahrenheit. In embodiments, the psilocybinextract includes an enthalpy of vaporization ranging from 80 kJ/mol to85 kJ/mol. In embodiments, the psilocybin extract includes an index ofrefraction ranging from 1.50 to 1.51, 1.51 to 1.52, 1.52 to 1.53, 1.53to 1.54, 1.54 to 1.55, 1.55 to 1.56, 1.56 to 1.57, 1.57 to 1.58, 1.58 to1.59, 1.59 to 1.60, 1.60 to 1.61, 1.61 to 1.62, 1.62 to 1.63, 1.63 to1.64, 1.64 to 1.65, 1.65 to 1.66, 1.66 to 1.67, 1.67 to 1.68, 1.68 to1.69, 1.69 to 1.70, 1.70 to 1.71, 1.71 to 1.72, 1.72 to 1.73, 1.73 to1.74, or 1.74 to 1.75.

In embodiments, the psilocybin extract includes a molar refractivityranging from: 4.00 cubic inches to 4.05 cubic inches, 4.05 cubic inchesto 4.10 cubic inches, 4.10 cubic inches to 4.15 cubic inches, 4.15 cubicinches to 4.20 cubic inches, 4.20 cubic inches to 4.25 cubic inches,4.25 cubic inches to 4.30 cubic inches, 4.30 cubic inches to 4.35 cubicinches, 4.35 cubic inches to 4.40 cubic inches, 4.40 cubic inches to4.45 cubic inches, 4.45 cubic inches to 4.50 cubic inches, 4.50 cubicinches to 4.55 cubic inches, 4.55 cubic inches to 4.60 cubic inches,4.60 cubic inches to 4.65 cubic inches, 4.65 cubic inches to 4.70 cubicinches, 4.70 cubic inches to 4.75 cubic inches, 4.75 cubic inches to4.80 cubic inches, 4.80 cubic inches to 4.85 cubic inches, 4.85 cubicinches to 4.90 cubic inches, 4.90 cubic inches to 4.95 cubic inches, or4.95 cubic inches to 5.00 cubic inches.

In embodiments, the psilocin extract includes a molecular weight rangingfrom 204.27 pounds per pound-mole and a melting point ranging from 343to 349 degrees Fahrenheit. In embodiments, the psilocin extract includesan index of refraction ranging from 1.50 to 1.51, 1.51 to 1.52, 1.52 to1.53, 1.53 to 1.54, 1.54 to 1.55, 1.55 to 1.56, 1.56 to 1.57, 1.57 to1.58, 1.58 to 1.59, 1.59 to 1.60, 1.60 to 1.61, 1.61 to 1.62, 1.62 to1.63, 1.63 to 1.64, 1.64 to 1.65, 1.65 to 1.66, 1.66 to 1.67, 1.67 to1.68, 1.68 to 1.69, 1.69 to 1.70, 1.70 to 1.71, 1.71 to 1.72, 1.72 to1.73, 1.73 to 1.74, or 1.74 to 1.75. In embodiments, the baeocystinextract includes a molecular weight ranging from 270.222 pounds perpound-mole. In embodiments, the norbaeocystin extract includes amolecular weight ranging from 256.19 pounds per pound-mole.

In embodiments, the psilocybin extract can be separated from thepsilocin extract by evaporation. In embodiments, the psilocybin extractcan be separated from the psilocin extract by a rotary evaporator,falling film tubular evaporator, rising/falling film tubular evaporator,rising film tubular evaporator, forced circulation evaporator, internalpump forced circulation evaporator, plate evaporator, evaporativecooler, multiple-effect evaporator, thermal vapor recompressionevaporator, mechanical vapor recompression evaporator, flash tank, acrystallizer, a draft tube and baffle crystallizer, coolingcrystallization, evaporative crystallization, fractionalcrystallization, and a distillation column. In embodiments, thepsilocybin extract can be separated from the psilocin extract by adifference in temperature. In embodiments, the psilocybin extract can beseparated from the psilocin extract by a difference in molecular weight.

In embodiments, the psilocybin extract is a crystalline solid having adensity ranging from between 68 pounds per cubic foot to 70 pounds percubic foot, 70 pounds per cubic foot to 72 pounds per cubic foot, 72pounds per cubic foot to 74 pounds per cubic foot, 74 pounds per cubicfoot to 76 pounds per cubic foot, 76 pounds per cubic foot to 78 poundsper cubic foot, 78 pounds per cubic foot to 80 pounds per cubic foot, 80pounds per cubic foot to 85 pounds per cubic foot, 85 pounds per cubicfoot to 90 pounds per cubic foot, 90 pounds per cubic foot to 100 poundsper cubic foot.

In embodiments, the psilocin extract is a crystalline solid having adensity ranging from between 68 pounds per cubic foot to 70 pounds percubic foot, 70 pounds per cubic foot to 72 pounds per cubic foot, 72pounds per cubic foot to 74 pounds per cubic foot, 74 pounds per cubicfoot to 76 pounds per cubic foot, 76 pounds per cubic foot to 78 poundsper cubic foot, 78 pounds per cubic foot to 80 pounds per cubic foot, 80pounds per cubic foot to 85 pounds per cubic foot, 85 pounds per cubicfoot to 90 pounds per cubic foot, 90 pounds per cubic foot to 100 poundsper cubic foot.

In embodiments, the baeocystin extract is a crystalline solid having adensity ranging from between 68 pounds per cubic foot to 70 pounds percubic foot, 70 pounds per cubic foot to 72 pounds per cubic foot, 72pounds per cubic foot to 74 pounds per cubic foot, 74 pounds per cubicfoot to 76 pounds per cubic foot, 76 pounds per cubic foot to 78 poundsper cubic foot, 78 pounds per cubic foot to 80 pounds per cubic foot, 80pounds per cubic foot to 85 pounds per cubic foot, 85 pounds per cubicfoot to 90 pounds per cubic foot, 90 pounds per cubic foot to 100 poundsper cubic foot.

In embodiments, the norbaeocystin extract is a crystalline solid havinga density ranging from between 68 pounds per cubic foot to 70 pounds percubic foot, 70 pounds per cubic foot to 72 pounds per cubic foot, 72pounds per cubic foot to 74 pounds per cubic foot, 74 pounds per cubicfoot to 76 pounds per cubic foot, 76 pounds per cubic foot to 78 poundsper cubic foot, 78 pounds per cubic foot to 80 pounds per cubic foot, 80pounds per cubic foot to 85 pounds per cubic foot, 85 pounds per cubicfoot to 90 pounds per cubic foot, 90 pounds per cubic foot to 100 poundsper cubic foot.

In embodiments, the esterified lipids (2D51) is then mixed with one ormore ingredients (2D64) selected from the group consisting of basil,bergamot, black pepper, cassia, cedarwood, cinnamon, citronella, clarysage, clove, coffee, cypress, eucalyptus, evening primrose, fennel, firneedle, frankincense, gardenia, geranium, ginger, grapefruit,helichrysum, hop, hyssop, jasmine, juniper berry, lavender, lemon,lemongrass, mandarin, marjoram, melaleuca, melissa, myrrh, neroli,orange, oregano, palo santo, patchouli, peppermint, pine, romanchamomile, rose, rosemary, sandalwood, spikenard, tea tree, thyme,turmeric, vetiver, wintergreen, and ylang ylang.

In embodiments, the esterified lipids (2D51) is then mixed with one ormore ingredients (2D64) selected from the group consisting ofcannabidiol, tetrahydrocannabinol, distilled THC, distilled CBD,concentrated volatiles, THC or CBD crystals, and a cannabinoid emulsion.

In embodiments, the melt point of the mixture of insect lipids and waxranges from 75.00 degrees Fahrenheit 77.50 Fahrenheit, 77.50 degreesFahrenheit 80.00 Fahrenheit, 80.00 degrees Fahrenheit 82.50 Fahrenheit,82.50 degrees Fahrenheit 85.00 Fahrenheit, 85.00 degrees Fahrenheit87.50 Fahrenheit, 87.50 degrees Fahrenheit 90.00 Fahrenheit, 90.00degrees Fahrenheit 92.50 Fahrenheit, 92.50 degrees Fahrenheit 95.00Fahrenheit, 95.00 degrees Fahrenheit 97.50 Fahrenheit, 97.50 degreesFahrenheit 100.00 Fahrenheit, 100.00 degrees Fahrenheit 102.50Fahrenheit, 102.50 degrees Fahrenheit 105.00 Fahrenheit, 105.00 degreesFahrenheit 107.50 Fahrenheit, 107.50 degrees Fahrenheit 110.00Fahrenheit, 110.00 degrees Fahrenheit 112.50 Fahrenheit, 112.50 degreesFahrenheit 115.00 Fahrenheit, 115.00 degrees Fahrenheit 117.50Fahrenheit, 117.50 degrees Fahrenheit 120.00 Fahrenheit, 120.00 degreesFahrenheit 122.50 Fahrenheit, 122.50 degrees Fahrenheit 125.00Fahrenheit, 125.00 degrees Fahrenheit 127.50 Fahrenheit, 127.50 degreesFahrenheit 130.00 Fahrenheit, 130.00 degrees Fahrenheit 132.50Fahrenheit, 132.50 degrees Fahrenheit 135.00 Fahrenheit, 135.00 degreesFahrenheit 137.50 Fahrenheit, 137.50 degrees Fahrenheit 140.00Fahrenheit, 140.00 degrees Fahrenheit 142.50 Fahrenheit, 142.50 degreesFahrenheit 145.00 Fahrenheit, 145.00 degrees Fahrenheit 147.50Fahrenheit, 147.50 degrees Fahrenheit 150.00 Fahrenheit, 150.00 degreesFahrenheit 152.50 Fahrenheit, 152.50 degrees Fahrenheit 155.00Fahrenheit, 155.00 degrees Fahrenheit 157.50 Fahrenheit, 157.50 degreesFahrenheit 160.00 Fahrenheit, 160.00 degrees Fahrenheit 162.50Fahrenheit, 162.50 degrees Fahrenheit 165.00 Fahrenheit, 165.00 degreesFahrenheit 167.50 Fahrenheit, 167.50 degrees Fahrenheit 170.00Fahrenheit, 170.00 degrees Fahrenheit 172.50 Fahrenheit, 172.50 degreesFahrenheit 175.00 Fahrenheit, 175.00 degrees Fahrenheit 177.50Fahrenheit, or 177.50 degrees Fahrenheit 180.00 Fahrenheit.

In embodiments, the kinematic viscosity of the mixture of insect lipidsand wax ranges from 2.8 centipoise to 3 centipoise, 3 centipoise to 3.2centipoise, 3.2 centipoise to 3.4 centipoise, 3.4 centipoise to 3.6centipoise, 3.6 centipoise to 3.8 centipoise, 3.8 centipoise to 4centipoise, 4 centipoise to 4.2 centipoise, 4.2 centipoise to 4.4, 4.4centipoise to 4.6 centipoise, 4.6 centipoise to 4.8 centipoise, 4.8centipoise to 5 centipoise, 5 centipoise to 5.2 centipoise, 5.2centipoise to 5.4 centipoise, 5.4 centipoise to 5.6 centipoise, 5.6centipoise to 5.8 centipoise, 5.8 centipoise to 6 centipoise, or 6centipoise to 6.2 centipoise.

In embodiments, the lipids are mixed with an oil at a mixing mass rationranging from 1 pound of insect lipids per 0.050 pounds of wax, 1 poundof insect lipids per 0.060 pounds of wax, 1 pound of insect lipids per0.070 pounds of wax, 1 pound of insect lipids per 0.080 pounds of wax, 1pound of insect lipids per 0.090 pounds of wax, 1 pound of insect lipidsper 0.100 pounds of wax, 1 pound of insect lipids per 0.110 pounds ofwax, 1 pound of insect lipids per 0.120 pounds of wax, 1 pound of insectlipids per 0.130 pounds of wax, 1 pound of insect lipids per 0.140pounds of wax, 1 pound of insect lipids per 0.150 pounds of wax, 1 poundof insect lipids per 0.160 pounds of wax, 1 pound of insect lipids per0.170 pounds of wax, 1 pound of insect lipids per 0.180 pounds of wax, 1pound of insect lipids per 0.190 pounds of wax, 1 pound of insect lipidsper 0.200 pounds of wax, 1 pound of insect lipids per 0.210 pounds ofwax, 1 pound of insect lipids per 0.220 pounds of wax, 1 pound of insectlipids per 0.230 pounds of wax, 1 pound of insect lipids per 0.240pounds of wax, or 1 pound of insect lipids per 0.250 pounds of wax.

In embodiments, glyceryl stearate is produced by direct esterificationof glycerol with stearic acid. In embodiments, the fatty acids describedherein may undergo direct esterification of glycerol. In embodiments,stearic acid is reacted with glycerol to produce glyceryl stearate. Inembodiments, stearic acid is reacted with glycerol to produce glycerylstearate in the presence of a catalyst.

In embodiments, stearic acid is reacted with glycerol to produceglyceryl stearate in the presence of a catalyst, the catalyst includes aprecious metal, more than one precious metal, gold, silver, platinum,rhodium, palladium, iridium, molybdenum, tungsten, nickel, cobalt,manganese, copper, titanium, silicon, vanadium, copper oxide, zeolite, asorbent, a molecular sieve, zirconia, alumina, monoclinic or stabilizedor doped zirconia, alkali-earth hexaaluminates, ceria, yittria,lanthanum, magnesium aluminate, promoted alumina, silica, ortitania.

In embodiments, stearic acid is reacted with glycerol to produceglyceryl stearate in the presence of a catalyst in a fixed bed reactor,a fluidized bed reactor, a reactor, a continuously stirred tank reactoras shown in FIG. 12D. In embodiments, heat is added or removed from thecatalyst during the esterification process with steam, cooling water, acoolant, a refrigerated coolant, and combinations thereof.

In embodiments, stearic acid is reacted with glycerol to produceglyceryl stearate in the presence of one or more ingredients selectedfrom the group consisting of alcohol, diglycerides, esters, ethanol,ethyl acetate, glycerin, glycerol, hexane, hydrocarbon, isopropylalcohol, methanol, monoglycerides, polyol, and a solvent.

In embodiments, glyceryl stearate is produced by direct esterificationof glycerol with stearic acid and one or more acids selected from thegroup consisting of abscic acid, acetic acid, ascorbic acid, benzoicacid, citric acid, formic acid, fumaric acid, hydrochloric acid, lacticacid, malic acid, nitric acid, organic acids, phosphoric acid, potassiumhydroxide, propionic acid, salicylic acid, sulfamic acid, sulfuric acid,and tartaric acid.

In embodiments, glyceryl stearate is produced by direct esterificationof glycerol with stearic acid and a caustic material including one ormore materials selected from the group consisting of an alkalinesubstance, sodium hydroxide, lye, caustic soda, an inorganic compoundwith formula NaOH, a caustic base and alkali.

In embodiments, the esterification reaction occurs at a temperatureranging from one or more temperature ranges selected from the groupconsisting of 50 degrees Fahrenheit to 100 degrees Fahrenheit, 100degrees Fahrenheit to 150 degrees Fahrenheit, 150 degrees Fahrenheit to200 degrees Fahrenheit, 200 degrees Fahrenheit to 250 degreesFahrenheit, 250 degrees Fahrenheit to 300 degrees Fahrenheit, 300degrees Fahrenheit to 350 degrees Fahrenheit, 350 degrees Fahrenheit to400 degrees Fahrenheit, 400 degrees Fahrenheit to 450 degreesFahrenheit, 450 degrees Fahrenheit to 500 degrees Fahrenheit, 500degrees Fahrenheit to 550 degrees Fahrenheit, 550 degrees Fahrenheit to600 degrees Fahrenheit, 600 degrees Fahrenheit to 650 degreesFahrenheit, 650 degrees Fahrenheit to 700 degrees Fahrenheit, 700degrees Fahrenheit to 750 degrees Fahrenheit, 750 degrees Fahrenheit to800 degrees Fahrenheit, 800 degrees Fahrenheit to 850 degreesFahrenheit, 850 degrees Fahrenheit to 900 degrees Fahrenheit, 900degrees Fahrenheit to 1000 degrees Fahrenheit.

In embodiments, the esterification reaction occurs at a reaction timeincluding one or more reaction durations selected from the groupconsisting of 1 second to 5 seconds, 5 seconds to 15 seconds, 15 secondsto 30 seconds, 30 seconds to 1 minute, 1 minute to 2 minutes, 2 minutesto 3 minutes, 3 minutes to 4 minutes, 4 minutes to 5 minutes, 5 minutesto 10 minutes, 10 minutes to 15 minutes, 15 minutes to 20 minutes, 20minutes to 25 minutes, 25 minutes to 30 minutes, 30 minutes to 35minutes, 35 minutes to 40 minutes, 40 minutes to 45 minutes, 45 minutesto 50 minutes, 50 minutes to 55 minutes, 55 minutes to 1 hours, 1 hoursto 1.25 hours, 1.25 hours to 1.5 hours, 1.5 hours to 1.75 hours, 1.75hours to 2 hours, 2 hours to 2.5 hours, 2.5 hours to 3 hours, 3 hours to3.5 hours, 3.5 hours to 4 hours, 4 hours to 4.5 hours, 4.5 hours to 5hours, 5 hours to 5.5 hours, 5.5 hours to 6 hours, 7 hours to 8 hours, 9hours to 10 hours, 11 hours to 12 hours, 13 hours to 14 hours, 15 hoursto 16 hours, 17 hours to 18 hours, 19 hours to 20 hours, 21 hours to 22hours, 23 hours to 24 hours, 25 hours to 26 hours, 27 hours to 28 hours,29 hours to 30 hours, 31 hours to 32 hours, 33 hours to 34 hours, 35hours to 36 hours, 37 hours to 38 hours, 39 hours to 40 hours, 41 hoursto 42 hours, 43 hours to 44 hours, 45 hours to 46 hours, 47 hours to 48hours, 49 hours to 50 hours, 51 hours to 52 hours, 53 hours to 54 hours,55 hours to 56 hours, 57 hours to 58 hours, 59 hours to 60 hours, 61hours to 62 hours, 63 hours to 64 hours, 65 hours to 66 hours, 67 hoursto 68 hours, 69 hours to 70 hours, or 71 hours to 72 hours.

In embodiments, the esterification reaction occurs at a reaction pHincluding one or more pH ranges selected from the group consisting of: 1to 1.2, 1.2 to 1.4, 1.4 to 1.6, 1.6 to 1.8, 1.8 to 2, 2 to 2.2, 2.2 to2.4, 2.4 to 2.6, 2.6 to 2.8, 2.8 to 3, 3 to 3.2, 3.2 to 3.4, 3.4 to 3.6,3.6 to 3.8, 3.8 to 4, 4 to 4.2, 4.2 to 4.4, 4.4 to 4.6, 4.6 to 4.8, 4.8to 5, 5 to 5.2, 5.2 to 5.4, 5.4 to 5.6, 5.6 to 5.8, 5.8 to 6, 6 to 6.2,6.2 to 6.4, 6.4 to 6.6, 6.6 to 6.8, 6.8 to 7, 7 to 7.1, 7.1 to 7.3, 7.3to 7.5, 7.5 to 7.7, 7.7 to 7.9, 7.9 to 8.1, 8.1 to 8.3, 8.3 to 8.5, 8.5to 8.7, 8.7 to 8.9, 8.9 to 9.1, 9.1 to 9.3, 9.3 to 9.5, 9.5 to 9.7, 9.7to 9.9, 9.9 to 10.1, 10.1 to 10.3, 10.3 to 10.5, 10.5 to 10.7, 10.7 to10.9, 10.9 to 11.1, 11.1 to 11.3, 11.3 to 11.5, 11.5 to 11.7, 11.7 to11.9, 11.9 to 12.1, 12.1 to 12.3, 12.3 to 12.5, 12.5 to 12.7, or 12.7 to12.9.

In embodiments, the esterification reaction requires energy in the formof electricity, power, or steam which is provided by the powerproduction systems recited and disclosed at length below. Electricitymay be provided to the esterification reaction from the power productionsystem as discussed in detail below.

In embodiments, stearic acid is reacted with glycerol to produceglyceryl stearate in the presence of a biocatalyst, the biocatalystincludes one or more biocatalysts selected from the group consisting ofan enzyme, casein protease, atreptogrisin A, flavorpro, peptidase,protease A, protease, Aspergillus oryzae, Bacillus subtilis, Bacilluslicheniformis, Aspergillus niger, Aspergillus melleus, Aspergilusoryzae, papain, Carica papaya, bromelain, Ananas comorus stem, amicroorganism, yeast, a fungus. In embodiments, the glyceryl stearate isthen mixed with treated water, the treated water is treated with one ormore water treatment units selected from the group consisting of anadsorbent, an ion-exchange resin, a catalyst, activated carbon, amembrane, and combinations thereof. In embodiments, the glycerylstearate is then mixed with one or more ingredients selected from thegroup consisting of alcohol, diglycerides, esters, ethanol, ethylacetate, glycerin, glycerol, hexane, hydrocarbon, isopropyl alcohol,methanol, monoglycerides, and a solvent. In embodiments, the glycerylstearate is then mixed with cannabis oil, wax, volatiles, a cannabinoid.In embodiments, the glyceryl stearate is then mixed with a terpeneincluding one or more terpenes selected from the group consisting oflimonene, humulene, pinene, linalool, caryophyllene, myrcene,eucalyptol, nerolidol, bisablol,

In embodiments, the insect oil is saponified. In embodiments, thehydrogenated insect oil is saponified. In embodiments, the insect oil issaponified and converted into a surfactant by reaction with an alkali.In embodiments, the alkali includes lye, sodium hydroxide, potassiumhydroxide, or combinations thereof. In embodiments, the type of alkalimetal used determines the kind of soap product. In embodiments, the soapincludes a sodium soap prepared from sodium hydroxide. In embodiments,the soap includes a potassium soap derived from potassium hydroxide. Inembodiments, the soap is hard, soft, or a liquid.

In embodiments, the presentdisclosure describes insect soaps which aresodium or potassium fatty acids salts, produced from the hydrolysis ofinsect lipids in a chemical reaction called saponification.

In embodiments, the insect oil is saponified and converted into asurfactant by reaction with an alkali. In embodiments, the insect oilsoap is a salt of a fatty acid. In embodiments, the insect oilsaponification is a process by which the fatty acids within the insectoil are reacted with sodium hydroxide or potassium hydroxide to produceglycerol and a fatty acid salt, called soap. In embodiments, the insectoil soap can be used as an insecticide to kills insects on contact andmaybe used for houseplants, vegetables, flowers, cannabis plants, andfruits. In embodiments, the insect oil soap can be used as aninsecticide to kill pests such as adelgids (woolly aphids), aphids,crickets, earwigs, grasshoppers, lacebugs, leafhoppers, mealybugs,mites, plant bugs, psyllids, sawfly larvae (pear slugs and/or roseslugs), scale insects, spider mites, tent caterpillars, thrips,whiteflies, and combinations thereof.

In embodiments, the soap has a hardness number, wherein the higher thehardness number the harder the soap. In embodiments, the hardness numberranges from 25 to 30, 30 to 35, 35 to 40, 40 to 45, 45 to 50, 50 to 55,55 to 60, 60 to 65, 65 to 70, 70 to 75, 75 to 80, 80 to 85, 85 to 90, 90to 95, 95 to 100. Example 1, insect soap with hardness of 30 to 55.Example 2, insect soap with hardness of 35 to 45. Example 3, insect soapwith hardness of 25 to 40. Example 4, insect soap with hardness of 45 to75.

In embodiments, the insect soap is fatty acids of a salt. Inembodiments, the insect soap is used as cleansers and lubricants. Inembodiments, the insect soap cleans by acting as a surfactant andemulsifier. In embodiments, the insect soap is a surfactant compoundsthat lowers the surface tension (or interfacial tension) between twoliquids, between a gas and a liquid, or between a liquid and a solid. Inembodiments, the insect soap is a surfactant whcih acts as a detergent,wetting agent, emulsifier, foaming agent, or dispersant. In embodiments,the insect soap is a surfactant compounds used in a pharmaceutical. Inembodiments, the insect soap is a surfactant compounds used in cosmeticproduct.

In embodiments, the insect soap is an insect surfactant. In embodiments,the insect surfactant can be used to produce insect-oil deriveddetergents, fabric softeners, emulsions, soaps, paints, adhesives, inks,anti-fogs, deinking of recycled papers, in enzymatic processes,laxatives. In embodiments, the insect surfactant can be used to produceinsect-oil derived agrochemical formulations such as herbicides,insecticides, biocides (sanitizers), and spermicides (nonoxynol-9). Inembodiments, the insect surfactant can be used to produce insect-oilderived personal care products such as cosmetics, acne medications,deodorants, shampoos, lotions, suntan lotions, sunscreen, sunblock,shower gel, hair conditioners (after shampoo), toothpastes.

In embodiments, the insect surfactant is an anionic surfactant. Inembodiments, the insect surfactant is a cationic surfactant. Inembodiments, the insect surfactant is a non-ionic surfactant. Inembodiments, the insect surfactant is an amphoteric surfactant. Inembodiments, theamphoteric surfactant is a surfactant thatsimultaneously carries both anionic and cationic hydrophilic groups withits structure containing simultaneously hermaphroditic ions which areable to form cation or anion according to the (such as pH changes)ambient conditions.

In embodiments, the insect surfactant can be used to produce insect-oilderived sunscreen, also known as sunblock, which may be lotion, spray,gel, foam (such as an expanded foam lotion or whipped lotion), stick orother topical product that absorbs or reflects some of the sun'sultraviolet (UV) radiation and thus helps protect against sunburn. Useof the insect-derived sunscreen can slow or temporarily prevent thedevelopment of wrinkles, dark spots and sagging skin. In embodiments,the insect derived sunscreen includes zinc oxide, titanium dioxide,which stay on the surface of the skin and mainly deflect the sunlight.In embodiments, the insect derived sunscreen includes a chemicalsunscreens which uses UV organic filters, which absorb the UV light, andmay or may not include oxybenzone, avobenzone, octisalate, octocrylene,homosalate and octinoxate. In embodiments, the insect derived sunscreenincludes oxybenzone, avobenzone, octisalate, octocrylene, homosalate andoctinoxate. In embodiments, the insect derived sunscreen includesbisoctrizole or2,2′-methanediylbis[6-(2H-benzotriazol-2-yl)-4-(2,4,4-trimethylpentan-2-yl)phenol]which has a CAS Number of 103597-45-1.

In embodiments, the insect surfactant can be used to produce insect-oilderived cannabis products. In embodiments, the insect surfactant can beused to produce insect-oil derived cannabinoid nanoemulsions. Inembodiments, the insect surfactant can be used to produce insect-oilderived terpene nanoemulsions. In embodiments, the insect surfactant canbe used to produce insect-oil nanoemulsions. In embodiments, the insectsurfactant can be used to produce insect-oil nanoemulsions includingpsilocybin extract, psilocin extract, baeocystin extract, and/ornorbaeocystin extract. In embodiments, the insect surfactant can be usedto produce insect-oil nanoemulsions including psilocybin, psilocin,baeocystin, and/or norbaeocystin. In embodiments, the insect surfactantcan be used to produce insect-oil nanoemulsions including ingredientsselected from the group consisting of ayahuasca, biologically activeorganic compound with four rings, a nootropic drug, acetate, activatedcharcoal, an amphetamine, ascorbic acid, aspirin, butyrate, calcium,capsaicin, carnitine, carnosine, cassia cinnamon, chondroitin sulfate,chromium, coenzyme q-10, cranberry, creatine, curcumin, deprenyl,dimethyltryptamine, echinacea, fish oil, garlic, ginger, ginkgo,ginseng, gluconic acid, glucosamine, green tea, hoodia, human growthhormone, 7-hydroxymitragynine, inositol, iowaska, kratom, lactic acid,lithium, lion's mane mushroom, lutein, magnesium, minerals, malate,melatonin, metformin, 3,4-methylenedioxymethamphetamine, milk thistle,n-acetylcysteine, niacin, niacinamide, nicotinamide riboside, omega-3fatty acid, oxaloacetate, piracetam, psilocybin, pyruvate, resveratrol,rhodiola, saw palmetto, selenium, St. john's wort, steroid alternatives,steroids, testosterone, theaflavins, turmeric, valerian, vitamins,vitamin B3, vitamin C, and zinc. In embodiments, the insect oil soap canbe diluted with treated water (as described in detail in other areas ofthe specification) and applied at a dilute solution to plants. Inembodiments, the insect oil soap can be diluted with treated water atsoap in water weight ratio ranging from: 0.1 to 0.2, 0.2 to 0.3, 0.3 to0.4, 0.4 to 0.5, 0.5 to 0.6, 0.6 to 0.7, 0.7 to 0.8, 0.8 to 0.9, 0.9 to1, 1 to 1.2, 1.2 to 1.4, 1.4 to 1.6, 1.6 to 1.8, 1.8 to 2, 2 to 2.5, 2.5to 3, 3 to 3.5, 3.5 to 4, 4 to 4.5, 4.5 to 5, 5 to 6, 6 to 7, 7 to 8, 8to 9, 9 to 10, 10 to 15, 15 to 20, 20 to 25, 25 to 30. In embodiments,the insect oil soap includes liquid soap, bar soap, kitchen soap,laundry soap, medicated soap, antibacterial soap. In embodiments, theinsect oil soap includes citronella, peppermint, lemongrass, cedarwoodor geranium.

EXAMPLE 1

Insect oil, bar, hard. Hard insect oil soap made using sodium hydroxide(NaOH) or lye. This hard soap is a good cleanser in hard water thatcontains magnesium, chloride, and calcium ions. Example 2: Insect oil,liquid, soft. Soft insect oil soap is made from using potassiumhydroxide (KOH) rather than sodium hydroxide. Example 3: Insect oil fromcrickets, bar, hard. Hard insect oil soap made using sodium hydroxide(NaOH) or lye. Example 4: Insect oil from crickets, liquid, soft. Softinsect oil soap is made from using potassium hydroxide (KOH) rather thansodium hydroxide. Example 5: Insect oil from black soldier fly larvae,bar, hard. Hard insect oil soap made using sodium hydroxide (NaOH) orlye. Example 6: Insect oil from black soldier fly larvae, liquid, soft.Soft insect oil soap is made from using potassium hydroxide (KOH) ratherthan sodium hydroxide.

In embodiments, the soap includes a fragrance, the fragrance includesone or more fragrances selected from the group consisting of apple,apricot, apple pie, argan, cinnamon, coconut milk, cinnamon-orange,chocolate, lemon-basil, cranberry, elderflower, orange blossom, grape,green tea, ground lemon, ground orange, ground vanilla, honey, jasminedream, chamomile, honeysuckle, cotton, coconut, cucumber, melon,lavender, lavender-honey, lotus-cherry blossom, mango, olive,grapefruit, patchouli, peppermint, rose petals, roses, sandalwood,orange, cannabis, tobacco, tomato leaves, verbena, figs, violets, wildcountry, wild roses.

In embodiments, this disclosure describes: a surfactant derived frominsects; wherein: the surfactant includes saponified insect lipids; thesurfactant includes an alkali; the surfactant includes a hard soap; thesurfactant includes a liquid soap; the surfactant includes sodiumhydroxide; the surfactant includes potassium hydroxide; the surfactantincludes a hard soap, the hard soap includes cannabidiol; the surfactantincludes a hard soap, the hard soap is derived from cannabis.

FIG. 13:

FIG. 13 shows a simplistic diagram illustrating a pathogen removalmodule that is configured to remove pathogens from at least a portion ofthe insects transferred from the insect evacuation module (3000). Insome embodiments, a water bath (1581) containing hot water (1582) may beused to remove pathogens from the insects. In embodiments, thetemperature of the water bath (1581) includes a water bath temperaturesensor (1583) that is configured to input or output a signal (1584) tothe computer. In embodiment, the water bath temperature sensor (1583)indicates that the water bath (1581) operates at a temperature rangingfrom between: about 120 degrees Fahrenheit to about 130 degreesFahrenheit; about 130 degrees Fahrenheit to about 140 degreesFahrenheit; about 140 degrees Fahrenheit to about 150 degreesFahrenheit; about 150 degrees Fahrenheit to about 160 degreesFahrenheit; about 160 degrees Fahrenheit to about 170 degreesFahrenheit; about 170 degrees Fahrenheit to about 180 degreesFahrenheit; about 180 degrees Fahrenheit to about 190 degreesFahrenheit; about 190 degrees Fahrenheit to about 200 degreesFahrenheit; and, about 200 degrees Fahrenheit to about 212 degreesFahrenheit.

In embodiments a heat exchanger (HX1580) heats the water (1582) withinthe water bath (1581). In embodiments a heat exchanger (HX1580) heatsthe water (1582) within the water bath (1581) to form hot water (1582).The steam for the heat exchanger is provided by the second steam supply(LCP) that is provided from FIG. 14L. In embodiments, a secondcondensate (LAR) is discharged from the heat exchanger (HX1580) and isprovided to the condensate tank (LAP) on FIG. 14L.

In embodiments a caustic material (CSTC) may be added to the water bath(1581). In embodiments, the caustic material (CSTC) is an alkalinesubstance, sodium hydroxide, lye, caustic soda, an inorganic compoundwith formula NaOH, a caustic base and alkali. In embodiments, the hotwater (1582) within the water bath (1581) contains a caustic material(CSTC).

In embodiments, the water bath (1581) containing caustic material (CSTC)operates at a temperature ranging from between: about 120 degreesFahrenheit to about 130 degrees Fahrenheit; about 130 degrees Fahrenheitto about 140 degrees Fahrenheit; about 140 degrees Fahrenheit to about150 degrees Fahrenheit; about 150 degrees Fahrenheit to about 160degrees Fahrenheit; about 160 degrees Fahrenheit to about 170 degreesFahrenheit; about 170 degrees Fahrenheit to about 180 degreesFahrenheit; about 180 degrees Fahrenheit to about 190 degreesFahrenheit; about 190 degrees Fahrenheit to about 200 degreesFahrenheit; about 200 degrees Fahrenheit to about 210 degreesFahrenheit; about 210 degrees Fahrenheit to about 215 degreesFahrenheit; about 215 degrees Fahrenheit to about 220 degreesFahrenheit; about 220 degrees Fahrenheit to about 225 degreesFahrenheit; about 225 degrees Fahrenheit to about 230 degreesFahrenheit; about 230 degrees Fahrenheit to about 235 degreesFahrenheit; about 235 degrees Fahrenheit to about 240 degreesFahrenheit; about 240 degrees Fahrenheit to about 245 degreesFahrenheit; about 245 degrees Fahrenheit to about 250 degreesFahrenheit; about 250 degrees Fahrenheit to about 255 degreesFahrenheit; about 255 degrees Fahrenheit to about 260 degreesFahrenheit; about 260 degrees Fahrenheit to about 265 degreesFahrenheit; about 265 degrees Fahrenheit to about 270 degreesFahrenheit; about 270 degrees Fahrenheit to about 275 degreesFahrenheit; about 275 degrees Fahrenheit to about 280 degreesFahrenheit; about 280 degrees Fahrenheit to about 285 degreesFahrenheit; and, about 285 degrees Fahrenheit to about 300 degreesFahrenheit.

In embodiments, the hot water (1582) within the water bath (1581)contains a caustic material (CSTC) at a water-to-caustic mass ratioranging from between 0.43 to 19. The water-to-caustic mass ratio isdefined as the weight percent of water (1582) within the water bath(1581) divided by the weight percent of caustic material (CSTC) withinthe water bath (1581). 30 weight percent water (1582) divided by 70weight percent caustic material (CSTC) is a water-to-caustic mass ratioof 0.43. 35 weight percent water (1582) divided by 65 weight percentcaustic material (CSTC) is a water-to-caustic mass ratio of 0.54. 40weight percent water (1582) divided by 60 weight percent causticmaterial (CSTC) is a water-to-caustic mass ratio of 0.67. 45 weightpercent water (1582) divided by 55 weight percent caustic material(CSTC) is a water-to-caustic mass ratio of 0.82. 50 weight percent water(1582) divided by 50 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 1.00. 55 weight percent water (1582)divided by 45 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 1.22. 60 weight percent water (1582)divided by 40 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 1.50. 65 weight percent water (1582)divided by 35 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 1.86. 70 weight percent water (1582)divided by 30 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 2.33. 75 weight percent water (1582)divided by 25 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 3.00. 80 weight percent water (1582)divided by 20 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 4.00. 85 weight percent water (1582)divided by 15 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 5.67. 90 weight percent water (1582)divided by 10 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 9.00. 95 weight percent water (1582)divided by 5 weight percent caustic material (CSTC) is awater-to-caustic mass ratio of 19.000.

In embodiments, caustic material (CSTC) mixed with the hot water (1582)within the water bath (1581) includes one of more from the groupselected from: 5 weight percent caustic material (CSTC) to 10 weightpercent caustic material (CSTC); 10 weight percent caustic material(CSTC) to 15 weight percent caustic material (CSTC); 15 weight percentcaustic material (CSTC) to 20 weight percent caustic material (CSTC) 20weight percent caustic material (CSTC) to 25 weight percent causticmaterial (CSTC); 25 weight percent caustic material (CSTC) to 30 weightpercent caustic material (CSTC); 30 weight percent caustic material(CSTC) to 35 weight percent caustic material (CSTC); 35 weight percentcaustic material (CSTC) to 40 weight percent caustic material (CSTC); 40weight percent caustic material (CSTC) to 45 weight percent causticmaterial (CSTC); 45 weight percent caustic material (CSTC) to 50 weightpercent caustic material (CSTC); 50 weight percent caustic material(CSTC) to 55 weight percent caustic material (CSTC); 55 weight percentcaustic material (CSTC) to 60 weight percent caustic material (CSTC); 60weight percent caustic material (CSTC) to 65 weight percent causticmaterial (CSTC); and, 65 weight percent caustic material (CSTC) to 70weight percent caustic material (CSTC).

In embodiments, caustic material (CSTC) mixed with the hot water (1582)and insects within the water bath (1581) have a pH selected from one ormore from the group consisting of: 7.1 to 7.3, 7.3 to 7.5, 7.5 to 7.7,7.7 to 7.9, 7.9 to 8.1, 8.1 to 8.3, 8.3 to 8.5, 8.5 to 8.7, 8.7 to 8.9,8.9 to 9.1, 9.1 to 9.3, 9.3 to 9.5, 9.5 to 9.7, 9.7 to 9.9, 9.9 to 10.1,10.1 to 10.3, 10.3 to 10.5, 10.5 to 10.7, 10.7 to 10.9, 10.9 to 11.1,11.1 to 11.3, 11.3 to 11.5, 11.5 to 11.7, 11.7 to 11.9, 11.9 to 12.1,12.1 to 12.3, 12.3 to 12.5, 12.5 to 12.7, and 12.7 to 12.9.

In embodiments, the caustic material (CSTC) that is mixed with the water(1582) contacts insects and promotes a deacetylation reaction of theexoskeleton of insects. In embodiments, the caustic material (CSTC) thatis mixed with the water (1582) contacts insects and promotes adeacetylation reaction of the N-acetylglucosamine portion of theinsects. In embodiments, the mixture of water (1582) and causticmaterial (CSTC) serves to remove a function acetyl group from theN-acetylglucosamine portion of the insects.

In embodiments, the mixture of water (1582) and caustic material (CSTC)serve to remove a function acetyl group from the N-acetylglucosamineportion of the insects to form chitosan. Chitosan has the uniquenumerical identifier assigned by is Chemical Abstracts Service (CAS)Number of 9012-76-4.

In embodiments, the mixture of water (1582) and caustic material (CSTC)serve to remove a function acetyl group from the N-acetylglucosamineportion of the insects to form a linear polysaccharide. In embodiments,the mixture of water (1582) and caustic material (CSTC) serve todepolymerize the N-acetylglucosamine portion of the insects to formdepolymerized insects. Depolymerization means to break a polymer downinto or other smaller units. A caustic material (CSTC) to removes thefunction acetyl group from the N-acetylglucosamine portion of theinsects and thus the N-acetylglucosamine portion of the insects isbroken down into a smaller molecule.

Biopolymers are polymers produced by living organisms. Insects areliving organisms. Chitosan is a polymer. Chitosan is a polycationiclinear polysaccharide. Polysaccharides are polymers. Polysaccharides arepolymeric carbohydrate molecules composed of long chains ofmonosaccharide units bound together by glycosidic linkages. Chitosan isa polymer that is formed from the deacetylation of insects that containchitin. Chitin is contained within the exoskeleton of insects. Chitin isa long-chain polymer of an N-acetylglucosamine, a derivative of glucose.Polycations are poly electrolytes. An electrolyte is a substance thatproduces an electrically conducting solution when dissolved in a polarsolvent, such as water. Chitosan is a polyelectrolyte. A polyelectrolyteis a polymer that bears an electrolyte group. A polyelectrolyte is apositively-charged polymer. Chitosan is a is a positively-chargedpolymer. Heating and mixing water (1582) with a caustic material (CSTC)and insects can produce a polyelectrolyte or a polymer that bears anelectrolyte group. In embodiments, linear polysaccharide includeschitosan. In embodiments, the pathogen-depleted insects (1570) mayinclude a biopolymer (1570′), or deacetylated insects (1570″).

In embodiments, the mixture of water (1582), caustic material (CSTC),and insects at a temperature ranging from 200 degrees Fahrenheit to 280degrees Fahrenheit and at a water-to-caustic mass ratio ranging frombetween 0.43 to 19 to produce a polycationic linear polysaccharide or abiopolymer. In embodiments, the mixture of water (1582), causticmaterial (CSTC), and insects can be operated at temperature ranging from200 degrees Fahrenheit to 280 degrees Fahrenheit and at awater-to-caustic mass ratio ranging from between 0.43 to 19 to produce apolyelectrolyte. In embodiments, the mixture of water (1582), causticmaterial (CSTC), and insects can be operated at temperature ranging from200 degrees Fahrenheit to 280 degrees Fahrenheit and at awater-to-caustic mass ratio ranging from between 0.43 to 19 to produce achitosan.

In embodiments, the mixture of water (1582), caustic material (CSTC),and insects at a temperature ranging from 200 degrees Fahrenheit to 280degrees Fahrenheit and at a caustic concentration ranging from 5 weightpercent to 70 weight percent to produce a polycationic linearpolysaccharide or a biopolymer. In embodiments, the mixture of water(1582), caustic material (CSTC), and insects can be operated attemperature ranging from 200 degrees Fahrenheit to 280 degreesFahrenheit and at a caustic concentration ranging from 5 weight percentto 70 weight percent to produce a polyelectrolyte. In embodiments, themixture of water (1582), caustic material (CSTC), and insects can beoperated at temperature ranging from 200 degrees Fahrenheit to 280degrees Fahrenheit and at a caustic concentration ranging from 5 weightpercent to 70 weight percent to produce a chitosan.

FIG. 14A:

FIG. 14A shows a simplistic diagram illustrating a multifunctionalcomposition mixing module that is configured to generate amultifunctional composition from at least a portion of the insectstransferred from the pathogen removal module and including the sequencesteps or sub-modules including an insect distribution module (6A),fiber-starch distribution module (6B), binding agent distribution module(6C), density improving textural supplement distribution module (6D),moisture improving textural supplement distribution module (6E),multifunctional composition mixing module (6F).

Insect Distribution Module (6A)

FIG. 14A displays an insect distribution module (6A) including an insecttank (6A2) that is configured to accept insects (6A1). The insect tank(6A2) has an interior (6A3), an insect input (6A4), an insect conveyor(6A5), and an insect conveyor output (6A6). The insect tank (6A2)accepts insects (6A1) to the interior (6A3) and regulates and controlsan engineered amount of insects (6A1) downstream to be mixed to form amultifunctional composition. The insect conveyor (6A5) has an integratedinsect mass sensor (6A7) that is configured to input and output a signal(6A8) to the computer (COMP). The insect conveyor motor (6A9) has acontroller (6A10) that is configured to input and output a signal (6A11)to the computer (COMP). The insect mass sensor (6A7), insect conveyor(6A5), and insect conveyor motor (6A9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of insect (6A1)via an insect transfer line (6A12).

Fiber-Starch Distribution Module (6B)

FIG. 14A displays a fiber-starch distribution module (6B) including afiber-starch tank (6B2) that is configured to accept fiber-starch (6B1).The fiber-starch tank (6B2) has an interior (6B3), a fiber-starch input(6B4), a fiber-starch conveyor (6B5), and a fiber-starch conveyor output(6B6). The fiber-starch tank (6B2) accepts fiber-starch (6B1) to theinterior (6B3) and regulates and controls an engineered amount offiber-starch (6B1) downstream to be mixed to form a multifunctionalcomposition. The fiber-starch conveyor (6B5) has an integratedfiber-starch mass sensor (6B7) that is configured to input and output asignal (6B8) to the computer (COMP). The fiber-starch conveyor motor(6B9) has a controller (6B10) that is configured to input and output asignal (6B11) to the computer (COMP). The fiber-starch mass sensor(6B7), fiber-starch conveyor (6B5), and fiber-starch conveyor motor(6B9) are coupled so as to permit the conveyance, distribution, oroutput of a precise flow of fiber-starch (6B1) via a fiber-starchtransfer line (6B12).

Binding Agent Distribution Module (6C)

FIG. 14A displays a binding agent distribution module (6C) including abinding agent tank (6C2) that is configured to accept a binding agent(6C1). The binding agent tank (6C2) has an interior (6C3), a bindingagent input (6C4), a binding agent conveyor (6C5), and a binding agentconveyor output (6C6). The binding agent tank (6C2) accepts bindingagent (6C1) to the interior (6C3) and regulates and controls anengineered amount of a binding agent (6C1) downstream to be mixed toform a multifunctional composition. The binding agent conveyor (6C5) hasan integrated binding agent mass sensor (6C7) that is configured toinput and output a signal (6C8) to the computer (COMP). The bindingagent conveyor motor (6C9) has a controller (6C10) that is configured toinput and output a signal (6C11) to the computer (COMP). The bindingagent mass sensor (6C7), binding agent conveyor (6C5), and binding agentconveyor motor (6C9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of binding agent (6C1) via abinding agent transfer line (6C12).

Density Improving Textural Supplement Distribution Module (6D)

FIG. 14A displays a density improving textural supplement distributionmodule (6D) including a density improving textural supplement tank (6D2)that is configured to accept a density improving textural supplement(6D1). The density improving textural supplement tank (6D2) has aninterior (6D3), a density improving textural supplement input (6D4), adensity improving textural supplement conveyor (6D5), and a densityimproving textural supplement conveyor output (6D6). The densityimproving textural supplement tank (6D2) accepts density improvingtextural supplement (6D1) to the interior (6D3) and regulates andcontrols an engineered amount of a density improving textural supplement(6D1) downstream to be mixed to form a multifunctional composition. Thedensity improving textural supplement conveyor (6D5) has an integrateddensity improving textural supplement mass sensor (6D7) that isconfigured to input and output a signal (6D8) to the computer (COMP).The density improving textural supplement conveyor motor (6D9) has acontroller (6D10) that is configured to input and output a signal (6D11)to the computer (COMP). The density improving textural supplement masssensor (6D7), density improving textural supplement conveyor (6D5), anddensity improving textural supplement conveyor motor (6D9) are coupledso as to permit the conveyance, distribution, or output of a preciseflow of density improving textural supplement (6D1) via a densityimproving textural supplement transfer line (6D12).

Moisture Improving Textural Supplement Distribution Module (6E)

FIG. 14A displays a moisture improving textural supplement distributionmodule (6E) including a moisture improving textural supplement tank(6E2) that is configured to accept a moisture improving texturalsupplement (6E1). The moisture improving textural supplement tank (6E2)has an interior (6E3), a moisture improving textural supplement input(6E4), a moisture improving textural supplement conveyor (6E5), and amoisture improving textural supplement conveyor output (6E6). Themoisture improving textural supplement tank (6E2) accepts a moistureimproving textural supplement (6E1) to the interior (6E3) and regulatesand controls an engineered amount of a moisture improving texturalsupplement (6E1) downstream to be mixed to form a multifunctionalcomposition. The moisture improving textural supplement conveyor (6E5)has an integrated moisture improving textural supplement mass sensor(6E7) that is configured to input and output a signal (6E8) to thecomputer (COMP). The moisture improving textural supplement conveyormotor (6E9) has a controller (6E10) that is configured to input andoutput a signal (6E11) to the computer (COMP). The moisture improvingtextural supplement mass sensor (6E7), moisture improving texturalsupplement conveyor (6E5), and moisture improving textural supplementconveyor motor (6E9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of moisture improving texturalsupplement (6E1) via a moisture improving textural supplement transferline (6E12).

Cannabis Enhancer Distribution Module (6G)

FIG. 14A displays a cannabis enhancer distribution module (6G) includinga cannabis enhancer tank (6G2) that is configured to accept a cannabisenhancer (6G1). The cannabis enhancer tank (6G2) has an interior (6G3),a cannabis enhancer input (6G4), a cannabis enhancer conveyor (6G5), anda cannabis enhancer conveyor output (6G6). The cannabis enhancer tank(6G2) accepts a cannabis enhancer (6G1) to the interior (6G3) andregulates and controls an engineered amount of a cannabis enhancer (6G1)downstream to be mixed to form a multifunctional composition. Thecannabis enhancer conveyor (6G5) has an integrated cannabis enhancermass sensor (6G7) that is configured to input and output a signal (6G8)to the computer (COMP). The cannabis enhancer conveyor motor (6G9) has acontroller (6G10) that is configured to input and output a signal (6G11)to the computer (COMP). The cannabis enhancer mass sensor (6G7),cannabis enhancer conveyor (6G5), and cannabis enhancer conveyor motor(6G9) are coupled so as to permit the conveyance, distribution, oroutput of a precise flow of cannabis enhancer (6G1) via a cannabisenhancer transfer line (6G12).

Multifunctional Composition Mixing Module (6F)

FIG. 14A displays a multifunctional composition mixing module (6F)including a multifunctional composition tank (6F1) that is configured toaccept a mixture including insects (6A1), fiber-starch (6B1), bindingagent (6C1), density improving textural supplement (6D1), moistureimproving textural supplement (6E1), and cannabis enhancer (6G1) via amultifunctional composition transfer line (6F0). The insects (6A1) maybe pathogen-depleted insects (1570) transferred from the pathogenremoval unit (1550) as depicted in FIG. 14A. FIG. 14B shows the insects(6A1) as ground separated insects (1500) transferred from the grinder(1250). The multifunctional composition tank (6F1) has an interior(6F2), a multifunctional composition tank input (6F3), screw conveyor(6F9), multifunctional composition output (6F10). The multifunctionalcomposition tank (6F1) accepts insects (6A1), fiber-starch (6B1),binding agent (6C1), density improving textural supplement (6D1),moisture improving textural supplement (6E1), and cannabis enhancer(6G1) to the interior (6F2) and mixes, regulates, and outputs a weighedmultifunctional composition stream (6F22).

The multifunctional composition tank (6F1) has a top section (6F4),bottom section (6F5), at least one side wall (6F6), with a level sensor(6F7) positioned thereon that is configured to input and output a signal(6F8) to the computer (COMP). The screw conveyor (6F9) has amultifunctional composition conveyor motor (6F11) with a controller(6F12) that is configured to input and output a signal (6F13) to thecomputer (COMP). From the multifunctional composition output (6F10) ofthe multifunctional composition tank (6F1) is positioned amultifunctional composition weigh screw (6F14) that is equipped with amultifunctional composition weigh screw input (6F15), a multifunctionalcomposition weigh screw output (6F16), and a mass sensor (6F17) that isconfigured to input and output a signal (6F18) to the computer (COMP).The multifunctional composition weigh screw (6F14) also has a weighscrew motor (6F19) with a controller (6F20) that is configured to inputand output a signal (6F21) to the computer (COMP).

FIG. 14B:

FIG. 14B shows a simplistic diagram illustrating a multifunctionalcomposition mixing module that is configured to generate amultifunctional composition as described in FIG. 14A however insteadfrom at least a portion of the insects transferred from the insectgrinding module.

FIG. 14C:

FIG. 14C shows one non-limiting embodiment of a liquid mixing module(LMM) that is configured to mix water with multifunctional composition(6F23) provided from the multifunctional composition mixing module asshown in FIG. 14A or 14B.

FIG. 14C shows one non-limiting embodiment of a liquid mixing module(LMM) that includes a first water treatment unit (C10), a second watertreatment unit (C11), and a third water treatment unit (C12), thatprovide a third contaminant depleted water (C13) to the interior (C14)of a mixing tank (C15). The mixing tank (C15) mixes a water supply (C16)with multifunctional composition (6F23) provided from themultifunctional composition mixing module as shown in FIG. 14A or 14B toform a multifunctional composition and water mixture (C17). Themultifunctional composition (6F23) introduced to the mixing tank (C15)may be a weighed multifunctional composition stream (6F22).

The multifunctional composition and water mixture (C17) is transferredfrom the mixing tank (C15) to the shaping module (14D) of FIG. 14D. Inembodiments, the multifunctional composition and water mixture (C17) istransferred and pressurized using a pump (C18) from the mixing tank(C15) to the shaping module (14D) of FIG. 14D. In embodiments, themultifunctional composition and water mixture (C17) is transferred andpressurized using a screw auger (C19) from the mixing tank (C15) to theshaping module (14D) of FIG. 14D.

FIG. 14C depicts the first water treatment unit (C10) to include acation, a second water treatment unit (C11) to include an anion, and athird water treatment unit (C13) to include a membrane. A first waterpressure sensor (C20) is positioned on the water input conduit (C21)that is introduced to the first input (C22) to the first water treatmentunit (C10). In embodiments, a filter (C23), activated carbon (C24),and/or an adsorbent (C25), are positioned on the water input conduit(C21) prior to introducing the water supply (C16) to the first watertreatment unit (C10). The water supply (C16) may be considered acontaminant-laden water (C26) that includes positively charged ions,negatively charged ions, and undesirable compounds. The positivelycharged ions are comprised of one or more from the group consisting ofcalcium, magnesium, sodium, and iron.

The negatively charged ions are comprised of one or more from the groupconsisting of iodine, chloride, and sulfate. The undesirable compoundsare comprised of one or more from the group consisting of dissolvedorganic chemicals, viruses, bacteria, and particulates.

In embodiments, the positively charged ions are comprised of one or morefrom the group consisting of calcium, magnesium, sodium, and iron. Inembodiments, the positively charged ions are comprised of one or morefrom the group consisting of aluminum, barium, beryllium, calcium,chromium(III), copper(I), copper(II), hydrogen, iron(II), iron(III),lead(II), lead(IV), lithium, magnesium, manganese(II), mercury(II),potassium, silver, sodium, strontium, tin(II), tin(IV), and zinc. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of iodine, chloride, and sulfate. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of acetate, aluminum silicate, anions fromorganic acids, azide, bromide, carbonate, chlorate, chloride, chromate,cyanide, dichromate, dihydrogen phosphate, fluoride, formate, hydride,hydrogen carbonate, hydrogen sulfate, hydrogen sulfite, hydroxide,hypochlorite, iodide, metasilicate, monohydrogen phosphate, nitrate,nitride, nitrite, oxalate, oxide, perchlorate, permanganate, peroxide,phosphate, silicate, sulfate, sulfide, sulfite, superoxide, andthiosulfate.

A first contaminant depleted water (C27) is discharged by the firstwater treatment unit (C10) by a first output (C28). The firstcontaminant depleted water (C27) may be a positively charged iondepleted water (C29). The first contaminant depleted water (C27) is thentransferred to the second water treatment unit (C11) via a second input(C30). A second contaminant depleted water (C31) is discharged by thesecond water treatment unit (C11) by a second output (C32). The secondcontaminant depleted water (C31) may be a negatively charged iondepleted water (C33). The second contaminant depleted water (C31) isthen transferred to the third water treatment unit (C12) via a thirdinput (C34). A third contaminant depleted water (C13) is discharged bythe third water treatment unit (C12) by a third output (C35). The thirdcontaminant depleted water (C13) may be an undesirable compoundsdepleted water (C36). The third contaminant depleted water (C13) is thentransferred to the interior (C14) of a mixing tank (C15) via a watersupply conduit (C37) and water input (C38).

Within the interior (C14) of a mixing tank (C15), the water is mixedwith multifunctional composition (6F23) provided from themultifunctional composition mixing module as shown in FIG. 14A or 14B.In embodiments, a cation (C39), an anion (C40), and a polishing unit(C41), are positioned on the water supply conduit (C37) in between thethird water treatment unit (C12) and the water input (C38) of the mixingtank (C15). The polishing unit (C41) may be any type of conceivabledevice to improve the water quality such as an ultraviolet unit, ozoneunit, microwave unit, filter, a distillation system or the like.

In embodiments, the mixing tank (C15) is equipped with a sensor (C44).In embodiments, the mixing tank (C15) is equipped with a first sensor(C44) and a second sensor (C45). The first sensor (C44) is used fordetecting a high level and the second sensor (C45) is used for detectinga low level. The first sensor (C44) is configured to output a signal tothe computer (COMP) when the first sensor (C44) is triggered by a highlevel of liquid within the mixing tank (C15). The second sensor (C45) isconfigured to output a signal to the computer (COMP) when the secondsensor (C45) is triggered by a low level of liquid within the mixingtank (C15). In embodiments, the mixing tank (C15) is equipped with asensor (C44) wherein the sensor includes a dialysis unit. Inembodiments, the dialysis unit is configured to remove toxins and/orwaste from the mixing tank (C15). In embodiments, the dialysis unitincludes at least one semipermeable membrane.

In embodiments, the insects (G56, G67) may include insect cells. Inembodiments, the insects (G56, G67) may include ovary cells from aninsect. In embodiments, the insects (G56, G67) may include cells from aninsect reproductive system. In embodiments, the insect cells areinfected with a baculovirus. In embodiments, the insect cells areinfected with a recombinant baculovirus. In embodiments, the insectcells are infected with a genetically engineered baculovirus.

In embodiments, feeding the baculovirus to the insects producesgenetically engineered insects, or transgenic insects. In embodiments,the transgenic insects are grown for a duration of time in theenvironmentally controlled IPSS to produce sufficient amounts ofinsect-derived antibodies and insect-derived lectins for separation andproduction of a variety of pharmaceutical compositions. In embodiments,the insect-derived antibodies and/or insect-derived lectins are purifiedinto a therapeutic pharmaceutical composition using a variety ofseparations.

FIG. 14G shows a mixing tank (G15). In embodiments, the mixing tank(G15) is a bioreactor (G15) equipped with an insect cell life supportsystem which includes at least one sensor (C44). In embodiments, theinsect cell life support system is configured to maintain the insectcells and keep them alive to allow the baculovirus to produce thepharmaceutical compositions. In embodiments, the bioreactor (G15) isequipped with a source of treated water provided to the bioreactor (G15)from the water treatment unit. In embodiments, the bioreactor (G15) isglass-lined or is made of glass.

In embodiments, the insect production system is configured as an insectcell baculovirus expression vector system (BEVS) to producepharmaceutical compositions including recombinant proteins.

In embodiments, the insect cells (G56, G67) introduced to the bioreactor(G15) of FIG. 14G include: cloned insect cells; polyclonal insect cells;polyclonal insect cells infected with a baculovirus; polyclonal insectcells infected with a recombinant baculovirus; polyclonal insect cellsinfected with a polyclonal recombinant baculovirus; polyclonal insectcells infected with an oligoclonal recombinant baculovirus; polyclonalinsect cells infected with a monoclonal recombinant baculovirus;oligoclonal insect cells; oligoclonal insect cells infected with abaculovirus; oligoclonal insect cells infected with a recombinantbaculovirus; oligoclonal insect cells infected with a polyclonalrecombinant baculovirus; oligoclonal insect cells infected with anoligoclonal recombinant baculovirus; oligoclonal insect cells infectedwith a monoclonal recombinant baculovirus; monoclonal insect cells;monoclonal insect cells infected with a baculovirus; monoclonal insectcells infected with a recombinant baculovirus; monoclonal insect cellsinfected with a polyclonal recombinant baculovirus; monoclonal insectcells infected with an oligoclonal recombinant baculovirus; and/ormonoclonal insect cells infected with a monoclonal recombinantbaculovirus.

In embodiments, the insect cells (G56, G67) within the bioreactor (G15)of FIG. 14G include: cloned insect cells; polyclonal insect cells;polyclonal insect cells infected with a baculovirus; polyclonal insectcells infected with a recombinant baculovirus; polyclonal insect cellsinfected with a polyclonal recombinant baculovirus; polyclonal insectcells infected with an oligoclonal recombinant baculovirus; polyclonalinsect cells infected with a monoclonal recombinant baculovirus;oligoclonal insect cells; oligoclonal insect cells infected with abaculovirus; oligoclonal insect cells infected with a recombinantbaculovirus; oligoclonal insect cells infected with a polyclonalrecombinant baculovirus; oligoclonal insect cells infected with anoligoclonal recombinant baculovirus; oligoclonal insect cells infectedwith a monoclonal recombinant baculovirus; monoclonal insect cells;monoclonal insect cells infected with a baculovirus; monoclonal insectcells infected with a recombinant baculovirus; monoclonal insect cellsinfected with a polyclonal recombinant baculovirus; monoclonal insectcells infected with an oligoclonal recombinant baculovirus; and/ormonoclonal insect cells infected with a monoclonal recombinantbaculovirus.

In embodiments, the insects (G56, G67) introduced to the bioreactor(G15) of FIG. 14G include: cloned insects; transgenic insects;genetically engineered insects; insects that are infected with arecombinant baculovirus; insects that are infected with a clonedrecombinant baculovirus; insects that are infected with a polyclonalrecombinant baculovirus; insects that are infected with an oligoclonalrecombinant baculovirus; and/or insects that are infected with amonoclonal recombinant baculovirus.

In embodiments, the insects (G56, G67) within the bioreactor (G15) ofFIG. 14G include: cloned insects; transgenic insects; geneticallyengineered insects; insects that are infected with a recombinantbaculovirus; insects that are infected with a cloned recombinantbaculovirus; insects that are infected with a polyclonal recombinantbaculovirus; insects that are infected with an oligoclonal recombinantbaculovirus; and/or insects that are infected with a monoclonalrecombinant baculovirus.

In embodiments, the insects and/or insect cells then produce a varietyof pharmaceutical compositions, including a cannabinoid, recombinantprotein, vaccine, antibody, peptide, or chemical and various othertherapeutics and cosmetic personal products from insects using high-techadvancements in bioprocessing, chemical, and controls, and automationengineering technologies. In embodiments, the chemical includes one ormore selected from the group consisting of cellular ribonucleic acid(RNA), ribosomal ribonucleic acid (RNA), messenger ribonucleic acid(RNA), transfer ribonucleic acid (RNA), competing endogenous RNA,microRNAs (miRNAs), messenger ribonucleic acid (mRNA), double-strandribonucleic acid (dsRNA), plasmid deoxyribonucleic acid, andcombinations thereof. In embodiments, the chemical includes abioinsecticide. In embodiments, the chemical includes an insecticide. Inembodiments, the chemical includes a fungicide.

FIG. 14G shows a mixing tank discloses bioreactor (G15) configured toproduce an insect-derived pharmaceutical composition from a source amixture of water and genetically engineered insects to realize abiopharmaceutical manufacturing system with increased productivity,selectivity, flexibility, and reduction of cost and simplicity using asingle use processing architecture.

In embodiments, the insect cell life support system includes a dialysisunit configured to remove contaminants away from the mixture of insectcells and treated water. In embodiments, a mixture of insect cells andtreated water are purified to extract the antibodies and/or lectins fromthe bioreactor (G15). In embodiments, the pharmaceutical compositions,including the recombinant proteins, antibodies, and/or lectins arepurified via chromatography purification, distillation, evaporation,adsorption, or crystallization. In embodiments, the insect-derivedcannabinoid, recombinant protein, vaccine, antibody, peptide, orchemical is purified via chromatography purification, distillation,evaporation, adsorption, or crystallization. In embodiments, thebioreactor (G15) contains one or more ingredients selected from thegroup consisting of methylenedioxymethamphetamine, psilocybin, psilocin,baeocystin, norbaeocystin, cannabidiol, tetrahydrocannabinol, distilledcannabidiol, distilled tetrahydrocannabinol, and combinations thereof.In embodiments, the pharmaceutical compositions produced in thebioreactor (G15) may be mixed with one or more ingredients selected fromthe group consisting of methylenedioxymethamphetamine, psilocybin,psilocin, baeocystin, norbaeocystin, cannabidiol, tetrahydrocannabinol,distilled cannabidiol, distilled tetrahydrocannabinol, and combinationsthereof.

In embodiments, water supply valve (C42) is positioned on the watersupply conduit (C37) in between the third water treatment unit (C12) andthe water input (C38) of the mixing tank (C15). The water supply valve(C42) is equipped with a controller (C43) that inputs or outputs asignal from a computer (COMP). In embodiments, the mixing tank (C15) isequipped with a high-level sensor (C44) and a second sensor (C45). Thefirst sensor (C44) is used for detecting a high level and the secondsensor (C45) is used for detecting a low level. The first sensor (C44)is configured to output a signal to the computer (COMP) when the firstsensor (C44) is triggered by a high level of liquid within the mixingtank (C15). The second sensor (C45) is configured to output a signal tothe computer (COMP) when the second sensor (C45) is triggered by a lowlevel of liquid within the mixing tank (C15).

In embodiments, when the second sensor (C45) sends a signal to thecomputer (COMP), the water supply valve (C42) on the water supplyconduit (C37) is opened and introduces water into the mixing tank (C15)until the first sensor (C44) is triggered thus sending a signal to thecomputer (COMP) to close the water supply valve (C42). This levelcontrol loop including the first sensor (C44) for detecting a high leveland a second sensor (C45) for detecting a lower level may be coupled tothe operation of the water supply valve (C42) for introducing a watersupply (C16) through a first water treatment unit (C10), a second watertreatment unit (C11), and a third water treatment unit (C12), to providea third contaminant depleted water (C13) to the interior (C14) of amixing tank (C15).

The mixing tank (C15) may be placed on a load cell (C46) for measuringthe mass of the tank. The mixing tank (C15) may be equipped with a mixer(C47) for mixing water with multifunctional composition (6F23). Themultifunctional composition (6F23) is introduced to the interior (C14)of the mixing tank (C15) via an input (C51). The mixer (C47) may be ofan auger or blade type that is equipped with a motor (C48). The mixingtank (C15) has a multifunctional composition and water mixture output(C49) that is connected to a discharge conduit (C50).

The discharge conduit (C50) is connected at one end to themultifunctional composition and water mixture output (C49) of the mixingtank (C15) and at another end to a supply pump (C18) or a screw auger(C19). The supply pump (C18) or a screw auger (C19) provides apressurized source of multifunctional composition and water mixture(C17) to the downstream shaping module (14D) as shown in FIG. 14D. Themultifunctional composition and water mixture (C17) may be a pressurizedmultifunctional composition and water mixture (C17A).

In embodiments, a flow sensor (C51) and/or a flow totalizer (C52) may beinstalled on the water supply conduit (C37) to determine the mass orvolume of water that is sent to the interior (C14) of the mixing tank(C15). In embodiments, the mixing tank (C15) is equipped with a heatexchanger (C53) to heat the mixture of water and multifunctionalcomposition. The heat exchanger (C53) may be electrically heated orprovided with a source of steam or hot oil. In embodiments, the heatexchanger (C53) accepts a third steam supply (LCT) that is provided byFIG. 14L. In embodiments, a third condensate (LAS) is discharged fromthe heat exchanger (C53) and is provided to the condensate tank (LAP) onFIG. 14L.

In embodiments, the mass of water or multifunctional composition withinthe mixing tank (C15) can be measured via the load cell (C46). Inembodiments, water can be added to the mixing tank (C15) and the mass ofwater is measured, following by adding the multifunctional compositionto the interior (C14) of the mixing tank (C15) to know the mass of thetotal mixture. The contents within the mixing tank (C15) can be mixedwith the mixer and optionally heated.

FIG. 14D:

FIG. 14D shows one non-limiting embodiment of a shaping module (14D)that is configured to shape the multifunctional composition and watermixture (C17) to produce a shaped multifunctional composition mixture(D10).

Many shaping technologies are available to shape the multifunctionalcomposition and water mixture (C17) including one or more from the groupconsisting of extrusion, sheeting rolling, and cutting rolls. Extrusionis a process used to create a shaped multifunctional composition mixture(D10) having a fixed cross-sectional profile. The die (D15) has a fixedcross-sectional profile and is configured to accept the multifunctionalcomposition and water mixture (C17) and press it into an extrudate(D11). The multifunctional composition and water mixture (C17) is pushedthrough a die of the desired cross-section to create an extrudate (D11)or a shaped multifunctional composition mixture (D10) which may then becooked in a cooking module (14E) as shown in FIG. 14E.

In embodiments, the shaping module (14D) includes an extrusion system(D12). In embodiments, the extrusion system (D12) includes an inputhopper (D13), an auger (D14), and a die (D15). The auger (D14) is drivenby a motor (D16). The multifunctional composition and water mixture(C17) is transferred from the liquid mixing module (LMM) as shown inFIG. 14C and provided to the input hopper (D13) of the extrusion system(D12).

The multifunctional composition and water mixture (C17) is transferredthrough the die (D15) by the rotating motion of an auger (D14). As themultifunctional composition and water mixture (C17) is pressed throughthe die (D15) by the auger (D14), friction causes at least a portion ofthe extrusion system (D12) to generate heat. In embodiments, thetemperature within the extrusion system (D12) can increase due to thefriction caused by formation of the extrudate (D11). This requires theextrusion system (D12) to require a source of coolant, such as coolingwater, to cool regulate temperature and prevent overheating. Inembodiments, the auger (D14) is cooled with a coolant.

The auger (D14) is equipped with a shaft (D17) and flights (D18) and isconfigured to applying pressure on the multifunctional composition andwater mixture (C17) sufficient to squeeze through the die (D15). Theshaped multifunctional composition mixture (D10) or an extrudate (D11)is discharged from the extrusion system (D12) via a extrudate output(D19). The extrusion system (D12) is equipped with a stand (D20) toelevate it off the ground.

The shaped multifunctional composition mixture (D10) or an extrudate(D11) is discharged from the extrusion system (D12) via a extrudateoutput (D19) and is transferred to a conveyor (D21). The conveyor (D21)transfers the extrudate (D11) to the cooking module (14E) as shown inFIG. 14E. The conveyor (D21) may be mechanical, pneumatic, air conveyor,elevating conveyor, conveyor belt, a drag-chain conveyor, bucketelevator, or any conceivable means to transfer extrudate (D11) from theextrusion system (D12) to the cooking module (14E).

In embodiments, the extrusion system (D12) is equipped with an extrusionpressure sensor (D21) that is configured to input or output a signal(D22) to the computer (COMP). In embodiments, the extrusion pressuresensor (D21) reads a pressure within the extrusion system (D12) rangingfrom: between about 0.25 PSI to about 49.99 PSI; between about 50 PSI toabout 99.99 PSI; between about 100 PSI to about 149.99 PSI; betweenabout 150 PSI to about 199.99 PSI; between about 200 PSI to about 249.99PSI; between about 250 PSI to about 299.99 PSI; between about 300 PSI toabout 349.99 PSI; between about 350 PSI to about 399.99 PSI; betweenabout 400 PSI to about 449.99 PSI; between about 450 PSI to about 499.99PSI; between about 500 PSI to about 549.99 PSI; between about 550 PSI toabout 599.99 PSI; between about 600 PSI to about 649.99 PSI; betweenabout 650 PSI to about 699.99 PSI; between about 700 PSI to about 749.99PSI; between about 750 PSI to about 799.99 PSI; between about 800 PSI toabout 8549.99 PSI; between about 850 PSI to about 899.99 PSI; betweenabout 900 PSI to about 949.99 PSI; between about 950 PSI to about 999.99PSI; between about 1,000 PSI to about 1,499.99 PSI; between about 1,500PSI to about 1,999.99 PSI; between about 2,000 PSI to about 2,499.99PSI; between about 2,500 PSI to about 2,999.99 PSI; between about 3,000PSI to about 3,499.99 PSI; between about 3,500 PSI to about 3,999.99PSI; between about 4,000 PSI to about 4,499.99 PSI; between about 4,500PSI to about 4,999.99 PSI; between about 5,000 PSI to about 5,499.99PSI; between about 5,500 PSI to about 5,999.99 PSI; between about 6,000PSI to about 6,499.99 PSI; between about 6,500 PSI to about 6,999.99PSI; between about 7,000 PSI to about 7,499.99 PSI; between about 7,500PSI to about 7,999.99 PSI; between about 8,000 PSI to about 8,499.99PSI; between about 8,500 PSI to about 8,999.99 PSI; between about 9,000PSI to about 9,499.99 PSI; between about 9,500 PSI to about 9,999.99PSI; between about 10,000 PSI to about 15,499.99 PSI; between about15,500 PSI to about 19,999.99 PSI; between about 20,000 PSI to about25,499.99 PSI; between about 25,500 PSI to about 29,999.99 PSI; betweenabout 30,000 PSI to about 35,499.99 PSI; and, between about 35,500 PSIto about 40,000 PSI.

It has been my realization that in one non-limiting embodiment the bestmode to operate the extrusion system (D12) includes maintaining theextrusion pressure sensor (D21) at a pressure less than 250 PSI.Nonetheless, all the above pressures may work as intended to realize ashaped multifunctional composition mixture (D10).

The extrusion system (D12) may be equipped with a coolant input (D23)and a coolant output (D24). A coolant input temperature sensor (D25) isconfigured to input and output a signal (D26) to the computer (COMP) andmeasures the temperature of coolant that passes into the coolant input(D23). A coolant output temperature sensor (D27) is configured to inputand output a signal (D28) to the computer (COMP) and measures thetemperature of coolant that leaves the coolant output (D24). A coolant(D29) passes from the coolant input (D23) to the coolant output (D24)and accepts heat from at least a portion of the extrusion system (D12).The temperature of the coolant (D29) measured at the coolant outputtemperature sensor (D27) is greater than the temperature measured by thecoolant input temperature sensor (D25).

In embodiments, the coolant input temperature sensor (D25) reads atemperature ranging from between about 60 degrees Fahrenheit to about150 degrees Fahrenheit. In embodiments, the coolant output temperaturesensor (D27) reads a temperature ranging from between about 150.999degrees Fahrenheit to about 210 degrees Fahrenheit.

FIG. 14E:

FIG. 14E shows one non-limiting embodiment of a cooking module (14E)that is configured to cook the shaped multifunctional compositionmixture (D10) provided from the shaping module (14D) to form a cookedmultifunctional composition mixture (E18A).

FIG. 14E shows one non-limiting embodiment of a cooking module (14E)that is configured to cook the shaped multifunctional compositionmixture (D10) or extrudate (D11) provided from the shaping module (14D)to form a cooked multifunctional composition mixture (E18A).

The cooking module (14E) as shown in FIG. 14E includes a cooking system(E10). The cooking system (E10) shown in FIG. 14D includes an oven (E11)or a fryer (E12). In embodiments, the fryer (E12) cooks the extrudate(D11) in an oil (E19). In embodiments, the oil (E19) are lipidsextracted from insects as shown in FIGS. 12A and/or 12B. In embodiments,the oil (E19) may be comprised of one or more from the group consistingof almond oil, animal-based oils, apricot kernel oil, avocado oil,brazil nut oil, butter, canola oil, cashew oil, cocoa butter, coconutoil, cooking oil, corn oil, cottonseed oil, fish oil, grapeseed oil,hazelnut oil, hemp oil, insect oil, lard, lard oil, macadamia nut oil,mustard oil, olive oil, palm kernel oil, palm oil, peanut oil, rapeseedoil, rice oil, rice bran oil, safflower oil, semi-refined sesame oil,semi-refined sunflower oil, sesame oil, soybean oil, tallow of beef,tallow of mutton, vegetable oil, and walnut oil.

In embodiments, the cooking system (E10) has a heat exchanger (E20) thatcooks the shaped multifunctional composition mixture (D10). Inembodiments, the heat exchanger (E20) accepts a fourth steam supply(LCX) that is provided from FIG. 14L. In embodiments, the heat exchanger(E20) outputs a fourth condensate (LAT) and is provided to thecondensate tank (LAP) on FIG. 14L. In embodiments, the fryer (E12) has aheat exchanger (E20) that heats an oil (E19) which in turn cooks theshaped multifunctional composition mixture (D10). In embodiments, theheat exchanger (E20) accepts a fourth steam supply (LCX) that isprovided from FIG. 14L. In embodiments, the heat exchanger (E20) outputsa fourth condensate (LAT) and is provided to the condensate tank (LAP)on FIG. 14L. The cooking system (E10) may also include a dryer (E13),pressure cooker (E14), dehydrator (E15), freeze dryer (E16), and mayoperate in a batch or continuous mode.

A conveyor (E17) may be integrated with the cooking system (E10). Theconveyor (E17) may be mechanical, pneumatic, air operated, an elevatingconveyor, conveyor belt, drag-chain conveyor, or the like.

The cooking system (E10) cooks the extrudate (D11) provided from theshaping module (14D) to form a cooked extrudate (E18) or a cookedmultifunctional composition mixture (E18A). The cooked extrudate (E18)or cooked multifunctional composition mixture (E18A) is transferred tothe flavoring module (14F) as shown in FIG. 14F. In embodiments, thecooked multifunctional composition mixture (E18A) is a cooked extrudate(E18).

In embodiments, the cooking system (E10) cooks the extrudate (D11) at atemperature ranging from between: 100 degrees F. to 124.99 degrees F.;125 degrees F. to 149.99 degrees F.; 150 degrees F. to 174.99 degreesF.; 175 degrees F. to 199.99 degrees F.; 200 degrees F. to 224.99degrees F.; 225 degrees F. to 249.99 degrees F.; 250 degrees F. to274.99 degrees F.; 275 degrees F. to 299.99 degrees F.; 300 degrees F.to 324.99 degrees F.; 325 degrees F. to 349.99 degrees F.; 350 degreesF. to 374.99 degrees F.; 375 degrees F. to 399.99 degrees F.; 400degrees F. to 550 degrees F.

In embodiments, the cooking system (E10) cooks the extrudate (D11) overa time duration ranging from between: 1 second to 5 seconds, 5 secondsto 15 seconds; 15 seconds to 30 seconds; 30 seconds to 1 minute; 1minute to 2 minutes; 2 minutes to 3 minutes; 3 minutes to 4 minutes; 4minutes to 5 minutes; 5 minutes to 6 minutes; 6 minutes to 7 minutes; 7minutes to 8 minutes; 8 minutes to 9 minutes; 9 minutes to 10 minutes;11 minutes to 12 minutes; 12 minutes to 13 minutes; 13 minutes to 14minutes; 14 minutes to 15 minutes; 15 minutes to 16 minutes; 16 minutesto 17 minutes; 17 minutes to 18 minutes; 18 minutes to 19 minutes; 19minutes to 60 minutes.

In embodiments, an air-oil heat exchanger (E21), an oil pump (E24),temperature sensor (E25), and a computer (E26) are integrated with thecooking system (E10). Hot oil (E19) is pumped from the fryer (E12) viaan oil pump (E24) to the air-oil heat exchanger (E21) where heat isremoved from the oil (E19) and transferred to the air (E23) by use of afan (E22) to heat the air (E23) that is located above the cooking system(E10).

In embodiments, the temperature sensor (E26) measures the temperature ofthe air (E23) above the cooking system (E10) and sends a signal (E27) tothe computer (COMP). A pre-determined air temperature is entered intothe computer (COMP) which may include one or more from the groupconsisting of 50 degrees Fahrenheit to 60 degrees Fahrenheit, 60 degreesFahrenheit to 70 degrees Fahrenheit, 70 degrees Fahrenheit to 80 degreesFahrenheit, and 80 degrees Fahrenheit to 90 degrees Fahrenheit.

When the temperature of the air (E23) located above the cooking system(E10) falls below the pre-determined air temperature, the computer(COMP) sends a signal (E28) to the motor (E29) of the oil pump (E24) topump oil (E19) to the air/oil heat exchanger (E21). Also, when thetemperature of the air (E23) located above the cooking system (E10)falls below the pre-determined air temperature, the computer (COMP)sends a signal (E30) to the motor (E31) of the fan (E22) to blow air(E23) across the surface of the air/oil heat exchanger (E21). This inturn transfer heat from the hot oil (E19) to the air (E23) that islocated above the cooking system (E10). The air/oil heat exchanger (E21)discharged cooled oil (E33) back to the fryer (E12) where to be mixedwith oil (E19) and heated using the fourth steam supply (LCX) that isprovided from FIG. 14L.

In embodiments, the cooking system (E10) shown in FIG. 14D can be usedto produce cooked-whole insects. In embodiments, whole insects may beintroduced to the cooking system (E10) shown in FIG. 14D to producecooked insects. In embodiments, the cooking system (E10) shown in FIG.14D can be used to produce cooked-whole insects from a source of heatedinsects. In embodiments, whole insects may be introduced to the cookingsystem (E10) shown in FIG. 14D to produce cooked insects from a sourceof heated insects. In embodiments, the cooking system (E10) shown inFIG. 14D can be used to produce cooked-whole insects from a source ofinsects that were submerged in a water bath. In embodiments, wholeinsects may be introduced to the cooking system (E10) shown in FIG. 14Dto produce cooked insects from a source of insects that were submergedin a water bath. In embodiments, the multifunctional composition mixture(D10) shown in FIG. 14E may comprise whole insects.

FIG. 14F:

FIG. 14F shows one non-limiting embodiment of a flavoring module (14F)that is configured to flavor the cooked multifunctional compositionmixture (E18A) provided from the cooking module (14E) to form a flavoredmultifunctional composition mixture (F10).

FIG. 14F shows one non-limiting embodiment of a flavoring module (14F)that is configured to flavor the cooked extrudate (E18) provided fromthe cooking module (14E) to form a flavored cooked extrudate (F10).

The flavoring module (14F) as shown in FIG. 14F includes a flavoringsystem (F11). The flavoring system (F11) shown in FIG. 14F includes aflavoring machine (F12) shown in the form of a tumbler (F13). Thetumbler (F13) has a motor (F14) and a controller (F15) and is configuredto be operated by a computer (COMP). The flavoring machine (F12) has acooked extrudate input (F16) for receiving the cooked extrudate (E18)from the cooking module (14E).

The flavoring machine (F12) has a flavoring input (F17) for receivingflavoring (F18). The flavoring (F18) are comprised of one or more fromthe group consisting of allspice berries, almond meal, anise seed,annato seed, arrowroot powder, basil, bay leaves, black pepper,buttermilk, cannabis, capsaicin, caraway, cayenne, celery seed, cheesecultures, chervil, Chile powder, chives, cilantro, cinnamon, citricacid, cloves, coconut shredded, coriander, corn oil, corn starch, creamof tartar, cubeb berries, cumin, curry, dextrose, dill, enzymes, fennel,fenugreek, file powder, garlic powder, ginger, grapefruit peel, greenpeppercorns, honey, horseradish powder, juniper berries, kaffir lime,lavender, lemon grass powder, lemon peel, lime peel, long pepper,marjoram, molasses, mustard, natural smoke flavor, nigella seeds,nutmeg, onion powder, orange peel, oregano, paprika, parsley,peppermint, poppy seed, powdered cheese, red pepper, rose petals,rosemary, saffron, sassafras, sage, salt, savory, sesame seed, staranise, sugar, sugar maple, sumac, tamarind, tangerine peel, tarragon,tetrahydrocannabinol, thyme, tomatillo powder, tomato powder, torulayeast, turmeric, vanilla extract, wasabi powder, whey, whitepeppercorns, yeast extract, and yeast.

In embodiments, the flavoring machine (F12) provides intimate contactbetween the flavoring (F18) and the cooked extrudate (E18) to form aflavored cooked extrudate (F10)

In embodiments, the flavoring machine (F12) provides intimate contactbetween the flavoring (F18) and the cooked multifunctional compositionmixture (E18A) to form a flavored multifunctional composition mixture(F10A). In embodiments, the tumbler (F13) rotates and provides intimatecontact between the flavoring (F18) and the cooked extrudate (E18) toform a flavored cooked extrudate (F10) or a flavored multifunctionalcomposition mixture (F10A). The flavoring machine (F12) has a flavoredcooked extrudate output (F19) for discharging the flavored cookedextrudate (F10) or flavored multifunctional composition mixture (F10A).In embodiments, the tumbler (F13) rotates at a revolution per minute(RPM) ranging from between: 3 RPM to 4 RPM; 4 RPM to 5 RPM; 6 RPM to 7RPM; 7 RPM to 8 RPM; 8 RPM to 9 RPM; 9 RPM to 10 RPM; 10 RPM to 11 RPM;11 RPM to 12 RPM; 13 RPM to 14 RPM; 14 RPM to 15 RPM; 15 RPM to 16 RPM;16 RPM to 17 RPM; 17 RPM to 18 RPM; 18 RPM to 19 RPM; 19 RPM to 20 RPM.

In embodiments, the flavored multifunctional composition mixture (F10A)is a flavored cooked extrudate (F10). A conveyor (F20) is equipped toaccept the flavored cooked extrudate (F10) from the flavored cookedextrudate output (F19). The conveyor (F20) may be mechanical, pneumatic,air operated, an elevating conveyor, conveyor belt, drag-chain conveyor,or any conceivable device to transport flavored multifunctionalcomposition mixture (F10) away from the flavoring machine (F12). Theconveyor (F20) may be equipped with a metal detector (F21). The metaldetector (F21) may be an electronic instrument which detects thepresence of metal within the flavored multifunctional compositionmixture (F10A).

FIG. 14G:

FIG. 14G shows one non-limiting embodiment of a biocatalyst mixingmodule (14G) that is configured to mix insects, water, biocatalyst, andoptionally acid to create an insect liquid biocatalyst mixture (G09).

FIG. 14G shows one non-limiting embodiment of a biocatalyst mixingmodule (14G) that includes a first water treatment unit (G10), a secondwater treatment unit (G11), and a third water treatment unit (G12), thatprovide a third contaminant depleted water (G13) to the interior (G14)of a mixing tank (G15). The mixing tank (G15) mixes a water supply (C16)with insects and biocatalyst. In embodiments, the insects introduced tothe mixing tank (G15) may be ground insects or whole insects. Inembodiments, the first water treatment unit (G10), a second watertreatment unit (G11), and a third water treatment unit (G12) areoptional. In embodiments, only one of the first water treatment unit(G10), second water treatment unit (G11), or third water treatment unit(G12) may be used. In embodiments, two of the first water treatment unit(G10), second water treatment unit (G11), or third water treatment unit(G12) may be used. In embodiments, a water supply (C16) is provided tothe interior (G14) of the mixing tank (G15). In embodiments, the mixingtank (G15) as shown in FIG. 14G (of Volume I) is the same vessel as theemulsion mixing tank (JLE) as shown in FIG. 17J′ (of Volume II).

In embodiments, the insects introduced to the mixing tank (G15) may be:(a) ground separated insects (1500) provided by the grinder (1250); (b)separated insects (334) from the separated insect conveyor (328); (c)insects (225) evacuated from the first feeding chamber (FC1) via theinsect evacuation output (205); (d) insects (225) evacuated from thefirst feeding chamber (FC1) via the insect evacuation output (205) andfeeding chamber exit conduit (302); and/or (e) insects removed from thefirst feeding chamber (FC1) via the conveyor output (249).

In embodiments, the insects introduced to the mixing tank (G15) may behave an insect bulk density ranging from between about 3.5 pounds percubic foot to about 14.999 pounds per cubic foot or a ground insect bulkdensity ranging from between about 15 pounds per cubic foot to about 50pounds per cubic foot.

The whole insects (G07) or ground insects (G08) introduced to the mixingtank (G15) may be a weighed. In embodiments, the whole insects (G07)introduced to the mixing tank (G15) may be have an insect bulk densityranging from between about 3.5 pounds per cubic foot to about 14.999pounds per cubic foot. In embodiments, the ground insects (G08) have aground insect bulk density ranging from between about 15 pounds percubic foot to about 50 pounds per cubic foot.

The insect liquid biocatalyst mixture (G09) is transferred from themixing tank (G15) to the exoskeleton separation module (14H) of FIG.14H. In embodiments, the insect liquid biocatalyst mixture (G09) istransferred and pressurized using a pump (G18) from the mixing tank(G15) to the exoskeleton separation module (14H) of FIG. 14H. Inembodiments, the insect liquid biocatalyst mixture (G09) is transferredand pressurized using a screw auger (G19) from the mixing tank (G15) tothe exoskeleton separation module (14H) of FIG. 14H.

FIG. 14G depicts the first water treatment unit (G10) to include acation, a second water treatment unit (G11) to include an anion, and athird water treatment unit (G13) to include a membrane. A first waterpressure sensor (G20) is positioned on the water input conduit (G21)that is introduced to the first input (G22) to the first water treatmentunit (G10). In embodiments, a filter (G23), activated carbon (G24),and/or an adsorbent (G25), are positioned on the water input conduit(G21) prior to introducing the water supply (G16) to the first watertreatment unit (G10). The water supply (G16) may be considered acontaminant-laden water (G26) that includes positively charged ions,negatively charged ions, and undesirable compounds. In embodiments, thepositively charged ions are comprised of one or more from the groupconsisting of calcium, magnesium, sodium, and iron. In embodiments, thepositively charged ions are comprised of one or more from the groupconsisting of aluminum, barium, beryllium, calcium, chromium(III),copper(I), copper(II), hydrogen, iron(II), iron(III), lead(II),lead(IV), lithium, magnesium, manganese(II), mercury(II), potassium,silver, sodium, strontium, tin(II), tin(IV), and zinc. In embodiments,the negatively charged ions are comprised of one or more from the groupconsisting of iodine, chloride, and sulfate. In embodiments, thenegatively charged ions are comprised of one or more from the groupconsisting of acetate, aluminum silicate, anions from organic acids,azide, bromide, carbonate, chlorate, chloride, chromate, cyanide,dichromate, dihydrogen phosphate, fluoride, formate, hydride, hydrogencarbonate, hydrogen sulfate, hydrogen sulfite, hydroxide, hypochlorite,iodide, metasilicate, monohydrogen phosphate, nitrate, nitride, nitrite,oxalate, oxide, perchlorate, permanganate, peroxide, phosphate,silicate, sulfate, sulfide, sulfite, superoxide, and thiosulfate. Theundesirable compounds are comprised of one or more from the groupconsisting of dissolved organic chemicals, viruses, bacteria, andparticulates.

A first contaminant depleted water (G27) is discharged by the firstwater treatment unit (G10) by a first output (G28). The firstcontaminant depleted water (G27) may be a positively charged iondepleted water (G29). The first contaminant depleted water (G27) is thentransferred to the second water treatment unit (G11) via a second input(G30). A second contaminant depleted water (G31) is discharged by thesecond water treatment unit (G11) by a second output (G32). The secondcontaminant depleted water (G31) may be a negatively charged iondepleted water (G33). The second contaminant depleted water (G31) isthen transferred to the third water treatment unit (G12) via a thirdinput (G34). A third contaminant depleted water (G13) is discharged bythe third water treatment unit (G12) by a third output (G35). The thirdcontaminant depleted water (G13) may be an undesirable compoundsdepleted water (G36). The third contaminant depleted water (G13) is thentransferred to the interior (G14) of a mixing tank (G15) via a watersupply conduit (G37) and water input (G38). In embodiments, a diptube(G38A) is provided to introduce water to beneath the liquid level of thecontents within the interior (G14) of the mixing tank (G15).

Within the interior (G14) of a mixing tank (G15), the water is mixedwith insects and biocatalyst. In embodiments, a cation (G39), an anion(G40), and a polishing unit (G41), are positioned on the water supplyconduit (G37) in between the third water treatment unit (G12) and thewater input (G38) of the mixing tank (G15). The polishing unit (G41) maybe any type of conceivable device to improve the water quality such asan ultraviolet unit, ozone unit, microwave unit, filter, a distillationsystem, or the like. In embodiments, the polishing unit (G41) may be adistillation system. In embodiments, the electrical conductivity of thetreated water treated by the distillation system includes one or moreselected from the group consisting of: 0.1 μS to 0.5 μS, 0.50 to 1.00μS, 1.00 μS to 1.25 μS, 1.25 μS to 1.50 μS, 1.50 μS to 1.75 μS, 1.75 μSto 2.00 μS, 2.00 μS to 2.25 μS, 2.25 μS to 2.50 μS, 2.50 μS to 2.75 μS,2.75 μS to 3.00 μS, 3.00 μS to 3.25 μS, 3.25 μS to 3.50 μS, 3.50 μS to3.75 μS, 3.75 μS to 4.00 μS, 4.00 μS to 4.25 μS, 4.25 μS to 4.50 μS,4.50 μS to 4.75 μS, 4.75 μS to 5.00 μS, 5.00 μS, to 5.25 μS, 5.250 to5.50 μS, 5.50 μS to 5.75 μS, 5.75 μS to 6.00 μS, 6.00 μS to 6.25 μS,6.25 μS to 6.50 μS, 6.50 μS to 6.75 μS, 6.75 μS to 7.00 μS, 7.00 μS to7.25 μS, 7.25 μS to 7.50 μS, 7.50 μS to 7.75 μS, 7.75 μS to 8.00 μS,8.00 μS to 8.25 μS, 8.25 μS to 8.50 μS, 8.50 μS to 8.75 μS, 8.75 μS to9.00 μS, 9.00 μS to 9.25 μS, 9.25 μS to 9.50 μS, 9.50 μS to 9.75 μS,9.75 μS to 10.00 μS. In embodiments, μS means μS per centimeter.

In embodiments, water supply valve (G42) is positioned on the watersupply conduit (G37) in between the third water treatment unit (G12) andthe water input (G38) of the mixing tank (G15). The water supply valve(G42) is equipped with a controller (G43) that inputs or outputs asignal from a computer (COMP). In embodiments, the mixing tank (G15) isequipped with a high-level sensor (G44) and a low-level sensor (G45).The high-level sensor (G44) is used for detecting a high level and thelow-level sensor (G45) is used for detecting a low level. The high-levelsensor (G44) is configured to output a signal to the computer (COMP)when the high-level sensor (G44) is triggered by a high level of liquidwithin the mixing tank (G15). The low-level sensor (G45) is configuredto output a signal to the computer (COMP) when the low-level sensor(G45) is triggered by a low level of liquid within the mixing tank(G15).

In embodiments, when the low-level sensor (G45) sends a signal to thecomputer (COMP), the water supply valve (G42) on the water supplyconduit (G37) is opened and introduces water into the mixing tank (G15)until the high-level sensor (G44) is triggered thus sending a signal tothe computer (COMP) to close the water supply valve (G42). This levelcontrol loop including the high-level sensor (G44) for detecting a highlevel and a low-level sensor (G45) for detecting a lower level may becoupled to the operation of the water supply valve (G42) for introducinga water supply (G16) through a first water treatment unit (G10), asecond water treatment unit (G11), and a third water treatment unit(G12), to provide a third contaminant depleted water (G13) to theinterior (G14) of a mixing tank (G15).

The mixing tank (GC15) may be placed on a load cell (G46) for measuringthe mass of the tank. The mixing tank (G15) may be equipped with a mixer(G47) for mixing water with insects and biocatalyst. The insects andbiocatalyst may be introduced to the interior (G14) of the mixing tank(G15) via an input (G51). The mixer (G47) may be of an auger or bladetype that is equipped with a motor (G48). The mixing tank (G15) has aninsect liquid biocatalyst mixture output (G49) that is connected to atransfer conduit (G50).

The transfer conduit (G50) is connected at one end to the insect liquidbiocatalyst mixture output (G49) of the mixing tank (G15) and at anotherend to a supply pump (G18) or a screw auger (G19). The supply pump (G18)or a screw auger (G19) provides a pressurized insect liquid biocatalystmixture (G09B) to the exoskeleton separation module (14H) of FIG. 14H.

In embodiments, a flow sensor (G51) and/or a flow totalizer (G52) may beinstalled on the water supply conduit (G37) to determine the mass orvolume of water that is sent to the interior (G14) of the mixing tank(G15). In embodiments, the mixing tank (G15) is equipped with a heatexchanger (G53) to heat the mixture of water, biocatalyst, and insects.The heat exchanger (G53) may be electrically heated or provided with aheat transfer medium such as a source of steam or hot oil.

The mixing tank (G15) may have a heating jacket (G53J) to serve thepurpose of the heat exchanger (G53). The mixing tank (G15) or bioreactormay have a heating jacket (G53J) and includes a cylindrical tank. Inembodiments, the cylindrical tank (G15) includes a length to diameterratio ranging from 2 to 5. The cylindrical tank (G15) includes a lengthto diameter ratio ranging from 1 to 2, 2 to 3, 3 to 4, 4 to 5, 5 to 6.In embodiments, the cylindrical tank (G15) is vertically oriented and ismounted on legs or brackets. In embodiments, the cylindrical tank (G15)is horizontally oriented and is mounted on legs or brackets. Inembodiments, the cylindrical tank (G15) is horizontally oriented and ismounted on a saddle support. In embodiments, the cylindrical tank (G15)is vertically oriented and has a flat bottom and/or a concretefoundation with a length to diameter ratio ranging from 0.5 to 1, 1 to1.5, 1.5 to 2, 2 to 2.5.

The mixing tank (G15) with a heating jacket (G53J) is a vessel that isdesigned for controlling the temperature of its contents, by using aheating jacket around the vessel through which a heat transfer medium(e.g.—steam) is circulated. The heating jacket (G53J) is a cavityexternal to the interior (G14) of the mixing tank (G15) that permits theuniform exchange of heat between the heat transfer medium circulating init and the walls of the mixing tank (G15). FIG. 14G shows the heatingjacket (G53J) installed over a portion of the mixing tank (G15) creatingan interior (G53J-1) having an annular space within which a heattransfer medium flows.

The heating jacket (G53J) has a heat transfer medium inlet (G90) and aheat transfer medium outlet (G91). Steam (G92) is introduced to the heattransfer medium inlet (G90). Steam condensate (G93) is discharged fromthe heat transfer medium outlet (G91). Steam (G92) is introduced to theheat transfer medium inlet (G90) of the heating jacket (G53J) of themixing tank (G15) via a steam inlet conduit (G94). The steam inletconduit (G94) is connected to the heat transfer medium inlet (G90) andis configured to transfer steam to the interior (G53J-1) of the heatingjacket (G53J).

In embodiments, a fifth steam supply (LDB) is provided to the heatingjacket (G53J) and/or to the heat exchanger (G53) and is provided fromFIG. 14L. In embodiments, the steam condensate (G93) that is dischargedfrom the heat transfer medium outlet (G91) is transferred to thecondensate tank (LAP) shown in FIG. 14L as a fifth condensate (LAU).

A steam supply valve (G95) is interposed on the steam inlet conduit(G94). The steam supply valve (G95) is equipped with a controller (G96)that inputs and outputs a signal (G97) to the computer (COMP). Inembodiments, the steam supply valve (G95) is positioned to regulate themass of heat transfer medium that leaves the heating jacket (G53J) viathe discharged from the heat transfer medium outlet (G91).

In embodiments, a temperature sensor (G54) measures the temperature ofthe contents within the interior (G14) of the mixing tank (G15). Thetemperature sensor (G54) is configured to output a signal (G55) to thecomputer (COMP). A pre-determined setpoint for the mixing tank (G15)temperature sensor (G54) may be inputted to the computer (COMP). Inresponse to the pre-determined setpoint, the computer (COMP) regulatesthe modulation of the steam supply valve (G95). The preferred modulationrange of the steam supply valve (G95) ranges from 33% open to 66% open.In embodiments, the preferred modulation range of the steam supply valve(G95) ranges from: 5% open to 10% open; 10% open to 15% open; 15% opento 20% open; 20% open to 30% open; 30% open to 40% open; 40% open to 50%open; 50% open to 60% open; 60% open to 70% open.

In embodiments, the mixing tank (G15) has a plurality of baffles (G55A,G55B) that are positioned within the interior (G14). Each baffle (G55A,G55B) is configured to promote mixing and increase heat transfer andchemical reaction rate of the biocatalyst with the insects.

The pressure drop across the steam supply valve (G95) ranges frombetween: 1 pound per square inch (PSI) to 2 PSI; 2 pounds per squareinch (PSI) to 5 PSI; 5 pounds per square inch (PSI) to 10 PSI; 10 poundsper square inch (PSI) to 20 PSI; 20 pounds per square inch (PSI) to 40PSI; 40 pounds per square inch (PSI) to 60 PSI; 60 pounds per squareinch (PSI) to 80 PSI; 80 pounds per square inch (PSI) to 100 PSI; 100pounds per square inch (PSI) to 125 PSI; 125 pounds per square inch(PSI) to 150 PSI; 150 pounds per square inch (PSI) to 200 PSI.

The velocity of steam in the steam inlet conduit (G94) ranges from: 35feet per second to 45 feet per second; 45 feet per second to 55 feet persecond; 55 feet per second to 65 feet per second; 65 feet per second to75 feet per second; 75 feet per second to 85 feet per second; 85 feetper second to 95 feet per second; 95 feet per second to 105 feet persecond; 105 feet per second to 115 feet per second; 115 feet per secondto 125 feet per second; 125 feet per second to 135 feet per second; 135feet per second to 145 feet per second; 145 feet per second to 155 feetper second; 155 feet per second to 175 feet per second. The velocity ofsteam condensate discharged from the heat transfer medium outlet (G91)is less than 3 feet per second.

In embodiments, the heat transfer medium inlet (G90) is comprised of oneor more from the group consisting of: a Class 150 flange, a Class 300flange, sanitary clamp fitting, national pipe thread, or compressionfitting. In embodiments, the heat transfer medium outlet (G91) iscomprised of one or more from the group consisting of: a Class 150flange, a Class 300 flange, sanitary clamp fitting, national pipethread, or compression fitting. In embodiments, the mixing tank (G15) iscomprised of stainless steel or carbon steel and may be ceramic orglass-lined. In embodiments, the heating jacket (G53J) is comprised ofstainless steel or carbon steel and may be ceramic or glass-lined.

In embodiments, the temperature of the water, insect, and biocatalystmixture within the interior (G14) of the mixing tank (G15) ranges frombetween: 50 degrees F. to 60 degrees F.; 60 degrees F. to 70 degrees F.;70 degrees F. to 80 degrees F.; 80 degrees F. to 90 degrees F.; 90degrees F. to 100 degrees F.; 100 degrees F. to 110 degrees F.; 110degrees F. to 120 degrees F.; 120 degrees F. to 130 degrees F.; 130degrees F. to 140 degrees F.; 140 degrees F. to 150 degrees F.; 150degrees F. to 160 degrees F.; 160 degrees F. to 170 degrees F.; 170degrees F. to 180 degrees F.; 180 degrees F. to 190 degrees F.; 190degrees F. to 200 degrees F.; 200 degrees F. to 212 degrees F.

In embodiments, the water, insect, and biocatalyst mixture may mixedwithin the interior (G14) of the mixing tank (G15) ranges from between:5 minutes to 10 minutes; 10 minutes to 20 minutes; 20 minutes to 30minutes; 30 minutes to 40 minutes; 40 minutes to 50 minutes; 50 minutesto 1 hour; 1 hour to 1.5 hours; 1.5 hour to 2 hours; 2 hour to 3 hours;3 hour to 4 hours; 4 hour to 5 hours; 5 hour to 6 hours; 6 hour to 12hours; 12 hour to 18 hours; 18 hour to 24 hours; 1 day to 2 days; 2 daysto 3 days; 3 days to 4 days; 4 days to 5 days; 5 days to 1 week.

In embodiments, the mass of water, biocatalyst, or insects within themixing tank (G15) can be measured via the load cell (G46). Inembodiments, water can be added to the mixing tank (G15) and the mass ofwater is measured, following by adding the insects and/or biocatalyst tothe interior (G14) of the mixing tank (G15) to know the mass of thetotal mixture. The contents within the mixing tank (G15) can be mixedwith the mixer and heated.

Whole Insect Distribution Module (14 g 1)

FIG. 14G displays a whole insect distribution module (14G1) including aninsect tank (G55) that is configured to accept whole insects (G56). Thewhole insects (G56) may be: (a) separated insects (334) from theseparated insect conveyor (328), (b) insects (225) evacuated from thefirst feeding chamber (FC1) via the insect evacuation output (205), (c)insects (225) evacuated from the first feeding chamber (FC1) via theinsect evacuation output (205) and feeding chamber exit conduit (302),and/or, (d) insects removed from the first feeding chamber (FC1) via theconveyor output (249), (e) transported though interstate commerce via atleast one vehicle having three or more axles and having an engine, (f)transported though interstate commerce via at least one vehicle havingtwo axles and having an internal combustion engine or battery powered.

The insect tank (G55) has an interior (G57), an insect input (G58), aninsect conveyor (G59), and an insect conveyor output (G60). The insecttank (G55) accepts whole insects (G56) to the interior (G57) andregulates and controls an engineered amount of whole insects (G56)downstream to be mixed in the mixing tank (G15). The insect conveyor(G59) has an integrated insect mass sensor (G61) that is configured toinput and output a signal (G61A) to the computer (COMP). The insectconveyor motor (G62) has a controller (G63) that is configured to inputand output a signal (G64) to the computer (COMP). The insect mass sensor(G61), insect conveyor (G59), and insect conveyor motor (G62) arecoupled so as to permit the conveyance, distribution, or output of aprecise flow of whole insects (G56) via a whole insect transfer line(G65).

Ground Insect Distribution Module (14 g 2)

FIG. 14G displays a ground insect distribution module (14G2) includingan insect tank (G66) that is configured to accept ground insects (G67).

In embodiments, the ground insects (G67) may come from FIG. 14I andinclude the liquid-depleted insects (150) that were filtered in thefilter (I11). In embodiments, the ground insects (G67) may come fromFIG. 14J and include the liquid-depleted insects (J10, J53) that weredischarged from the evaporator (J11). In embodiments, the ground insects(G67) may come from FIG. 14K and include the third separated insects orfourth separated insects (KCX). In embodiments, the ground insects (G67)may come from FIG. 14K and include the third separated insects or fourthseparated insects (KCX). In embodiments, the ground insects (G67) maycome from FIG. 14K and include the small insect particulate portion(KCW) or the large insect particulate portion (KCY) that had undergoneevaporation by spray drying.

The ground insects (G67) may be: (a) ground separated insects (1500)provided by the grinder (1250), or (b) insects purchased throughinterstate commerce, (c) transported though interstate commerce via atleast one vehicle having three or more axles and having an internalcombustion engine, (d) transported though interstate commerce via atleast one vehicle having two axles and having an internal combustionengine or battery powered.

The insect tank (G66) has an interior (G68), an insect input (G69), aninsect conveyor (G70), and an insect conveyor output (G71). The insecttank (G66) accepts ground insects (G67) to the interior (G68) andregulates and controls an engineered amount of ground insects (G67)downstream to be mixed in the mixing tank (G15). The insect conveyor(G70) has an integrated insect mass sensor (G72) that is configured toinput and output a signal (G73) to the computer (COMP). The insectconveyor motor (G74) has a controller (G75) that is configured to inputand output a signal (G76) to the computer (COMP). The insect mass sensor(G72), insect conveyor (G70), and insect conveyor motor (G74) arecoupled so as to permit the conveyance, distribution, or output of aprecise flow of ground insects (G67) via a ground insect transfer line(G77).

Biocatalyst Distribution Module (14 g 3)

FIG. 14G displays a biocatalyst mixing module (14G3) including abiocatalyst tank (G78) that is configured to accept at least onebiocatalyst (G79). The biocatalyst (G79) may be comprised of one or morefrom the group consisting of an enzyme, casein protease, atreptogrisinA, flavorpro, peptidase, protease A, protease, Aspergillus oryzae,Bacillus subtilis, Bacillus licheniformis, Aspergillus niger,Aspergillus melleus, Aspergilus oryzae, papain, Carica papaya,bromelain, ananas comorus stem, and yeast, and mixtures of two and threeand four and more. In embodiments, mixing of the biocatalyst (G79) isoptional.

In embodiments, the biocatalyst includes yeast. In embodiments, theyeast may be ale yeast, the “top-fermenting” type, Saccharomycescerevisiae. In embodiments, the yeast may be lager yeast, the“bottom-fermenting” type, Saccharomyces uvarum, or Saccharomycescarlsbergensis. In embodiments, the yeast is liquid or powder. Yeastsare eukaryotic, single-celled microorganisms classified as members ofthe fungus kingdom.

In embodiments, the insects may be mixed with water, a biocatalyst,cannabis, and grain, barley, honey, and/or hops. In embodiments, thewater, a biocatalyst, optionally cannabis, and at least one from thegroup consisting of grain, barley, honey, and hops may be fermented toproduce ethyl alcohol. In embodiments, the water, a biocatalyst,optionally cannabis, and at least one from the group consisting ofgrain, barley, honey, and hops may be fermented to produce ethanol.

In embodiments, the water, a biocatalyst, optionally cannabis, and atleast one from the group consisting of malt, grain, barley, honey, andhops may be fermented to produce a mixture of water and ethanol. Alcoholby volume (abbreviated as ABV, abv, or alc/vol) is a standard measure ofhow much ethanol is contained in a given volume of an alcoholic beverage(expressed as a volume percent). In embodiments, the mixture of waterand ethanol has a range of alcohol by volume that is selected from oneor more from the group consisting of 2.5 ABV to 3 ABV, 3 ABV to 3.5 ABV,3.5 ABV to 4 ABV, 4 ABV to 4.5 ABV, 4.5 ABV to 5 ABV, 5 ABV to 5.5 ABV,5.5 ABV to 6 ABV, 6 ABV to 6.5 ABV, 6.5 ABV to 7 ABV, 7 ABV to 7.5 ABV,7.5 ABV to 8 ABV, 8 ABV to 8.5 ABV, 8.5 ABV to 9 ABV, 9 ABV to 9.5 ABV,9.5 ABV to 10 ABV, 10 ABV to 10.5 ABV, 10.5 ABV to 11 ABV, 11 ABV to11.5 ABV, 11.5 ABV to 12 ABV, and 12 ABV to 12.5 ABV.

In embodiments, the beverage has a serving size of 0.10 fluid ounce to0.5 fluid ounces, 0.50 fluid ounce to 1 fluid ounce, 1.0 fluid ounce to1.5 fluid ounces, 1.5 fluid ounce to 2.0 fluid ounces, 2.0 fluid ounceto 2.5 fluid ounces, 2.5 fluid ounce to 3.0 fluid ounces, 3.0 fluidounce to 3.5 fluid ounces, 3.5 fluid ounce to 4.0 fluid ounces, 4.0fluid ounce to 4.5 fluid ounces, 4.5 fluid ounce to 5.0 fluid ounces,5.0 fluid ounce to 5.5 fluid ounces, 5.5 fluid ounce to 6 fluid ounces,6 fluid ounces, 8 fluid ounces or 12 fluid ounces. In embodiments, thebeverage has a serving size of 1 fluid ounce to 2 fluid ounces, 2 fluidounces to 3 fluid ounces, 3 fluid ounces to 4 fluid ounces, 4 fluidounces to 5 fluid ounces, 5 fluid ounces to 6 fluid ounces, 6 fluidounces to 7 fluid ounces, 7 fluid ounces to 8 fluid ounces, 8 fluidounces to 9 fluid ounces, 9 fluid ounces to 10 fluid ounces, 10 fluidounces to 11 fluid ounces, 11 fluid ounces to 12 fluid ounces, 12 fluidounces to 13 fluid ounces, 13 fluid ounces to 14 fluid ounces, 14 fluidounces to 15 fluid ounces, 15 fluid ounces to 16 fluid ounces, 16 fluidounces to 17 fluid ounces, 17 fluid ounces to 18 fluid ounces, 18 fluidounces to 19 fluid ounces, 19 fluid ounces to 20 fluid ounces, 20 fluidounces to 21 fluid ounces, 21 fluid ounces to 22 fluid ounces, 22 fluidounces to 24 fluid ounces, 24 fluid ounces to 26 fluid ounces, 26 fluidounces to 28 fluid ounces, 28 fluid ounces to 30 fluid ounces, 30 fluidounces to 32 fluid ounces, 32 fluid ounces to 34 fluid ounces, 34 fluidounces to 36 fluid ounces, 36 fluid ounces to 38 fluid ounces, or 38fluid ounces to 40 fluid ounces.

In embodiments, each serving size of the beverage includes a cannabidiolcontent in milligrams per serving ranging from 0 milligrams to 0.5milligrams, 0.5 milligrams to 1 milligrams, 1 milligrams to 1.5milligrams, 1.5 milligrams to 2 milligrams, 2 milligrams to 2.5milligrams, 2.5 milligrams to 3 milligrams, 3 milligrams to 3.5milligrams, 3.5 milligrams to 4 milligrams, 4 milligrams to 4.5milligrams, 4.5 milligrams to 5 milligrams, 5 milligrams to 5.5milligrams, 5.5 milligrams t 6 milligrams, 6 milligrams to 6.5milligrams, 6.5 milligrams to 7 milligrams, 7 milligrams to 7.5milligrams, 7.5 milligrams to 8 milligrams, 8 milligrams to 8.5milligrams, 8.5 milligrams to 9 milligrams, 9 milligrams to 9.5milligrams, 9.5 milligrams to 10 milligrams, 10 milligrams to 11milligrams, 11 milligrams to 12 milligrams, 12 milligrams to 13milligrams, 13 milligrams to 14 milligrams, 14 milligrams to 15milligrams, 15 milligrams to 16 milligrams, 16 milligrams to 17milligrams, 17 milligrams to 18 milligrams, 18 milligrams to 19milligrams, 19 milligrams to 20 milligrams, 20 milligrams to 25milligrams, 25 milligrams to 30 milligrams, 30 milligrams to 35milligrams, 35 milligrams to 40 milligrams, 40 milligrams to 45milligrams, 45 milligrams to 50 milligrams, 50 milligrams to 60milligrams, 60 milligrams to 70 milligrams, 70 milligrams to 80milligrams, 80 milligrams to 90 milligrams, 90 milligrams to 100milligrams, 100 milligrams to 125 milligrams, 125 milligrams to 150milligrams, 150 milligrams to 175 milligrams, 175 milligrams to 200milligrams, 200 milligrams to 250 milligrams, 250 milligrams to 300milligrams, 300 milligrams to 350 milligrams, 350 milligrams to 400milligrams, 400 milligrams to 450 milligrams, or 450 milligrams to 500milligrams.

In embodiments, each serving size of the beverage includes atetrahydrocannabinol content in milligrams per serving ranging from 0milligrams to 0.5 milligrams, 0.5 milligrams to 1 milligrams, 1milligrams to 1.5 milligrams, 1.5 milligrams to 2 milligrams, 2milligrams to 2.5 milligrams, 2.5 milligrams to 3 milligrams, 3milligrams to 3.5 milligrams, 3.5 milligrams to 4 milligrams, 4milligrams to 4.5 milligrams, 4.5 milligrams to 5 milligrams, 5milligrams to 5.5 milligrams, 5.5 milligrams t 6 milligrams, 6milligrams to 6.5 milligrams, 6.5 milligrams to 7 milligrams, 7milligrams to 7.5 milligrams, 7.5 milligrams to 8 milligrams, 8milligrams to 8.5 milligrams, 8.5 milligrams to 9 milligrams, 9milligrams to 9.5 milligrams, 9.5 milligrams to 10 milligrams, 10milligrams to 11 milligrams, 11 milligrams to 12 milligrams, 12milligrams to 13 milligrams, 13 milligrams to 14 milligrams, 14milligrams to 15 milligrams, 15 milligrams to 16 milligrams, 16milligrams to 17 milligrams, 17 milligrams to 18 milligrams, 18milligrams to 19 milligrams, 19 milligrams to 20 milligrams, 20milligrams to 25 milligrams, 25 milligrams to 30 milligrams, 30milligrams to 35 milligrams, 35 milligrams to 40 milligrams, 40milligrams to 45 milligrams, 45 milligrams to 50 milligrams, 50milligrams to 60 milligrams, 60 milligrams to 70 milligrams, 70milligrams to 80 milligrams, 80 milligrams to 90 milligrams, 90milligrams to 100 milligrams, 100 milligrams to 125 milligrams, 125milligrams to 150 milligrams, 150 milligrams to 175 milligrams, 175milligrams to 200 milligrams, 200 milligrams to 250 milligrams, 250milligrams to 300 milligrams, 300 milligrams to 350 milligrams, 350milligrams to 400 milligrams, 400 milligrams to 450 milligrams, or 450milligrams to 500 milligrams.

In embodiments, the beverage has zero calories per serving size. Inembodiments, the beverage has a calories per serving ranging from 0 to1, 1 to 2, 2 to 3, 3 to 4, 4 to 5, 5 to 6, 6 to 7, 7 to 8, 8 to 9, 9 to10 to 15, 15 to 20, 20 to 25, 25 to 30, 30 to 35, 35 to 40, 40 to 45, 45to 50, 50 to 55, 55 to 60, 60 to 65, 65 to 70, 70 to 75, 75 to 80, 80 to85, 85 to 90, 90 to 95, 95 to 100, 100 to 110, 110 to 120, 120 to 130,130 to 140, 140 to 150, 150 to 160, 160 to 170, 170 to 180, 180 to 190,190 to 200, 200 to 210, 210 to 220, 220 to 230, 230 to 240, 240 to 250,250 to 260, 260 to 270, 270 to 280, 280 to 290, 290 to 300, or 300 to310.

In embodiments, the beverage has a sodium content (in milligrams perserving) ranging from 0 to 1, 1 to 2, 2 to 3, 3 to 4, 4 to 5, 5 to 6, 6to 7, 7 to 8, 8 to 9, 9 to 10, 10 to 11, 11 to 12, 12 to 13, 13 to 14,14 to 15, 15 to 16, 16 to 17, 17 to 18, 18 to 19, 19 to 20, 20 to 25, 25to 30, 30 to 35, 35 to 40, 40 to 45, 45 to 50, 50 to 55, 55 to 60, 60 to65, 65 to 70, 70 to 75, 75 to 80, 80 to 85, 85 to 90, 90 to 95, 95 to100.

In embodiments, the beverage has a carbohydrate content (in grams perserving) ranging from 0 to 1, 1 to 2, 2 to 3, 3 to 4, 4 to 5, 5 to 6, 6to 7, 7 to 8, 8 to 9, 9 to 10, 10 to 11, 11 to 12, 12 to 13, 13 to 14,14 to 15, 15 to 16, 16 to 17, 17 to 18, 18 to 19, 19 to 20, 20 to 25, 25to 30, 30 to 35, 35 to 40, 40 to 45, 45 to 50, 50 to 55, 55 to 60, 60 to65, 65 to 70, 70 to 75, 75 to 80, 80 to 85, 85 to 90, 90 to 95, 95 to100.

In embodiments, the beverage includes aspartame, sodium, sodiumchloride, sucrose, sugar, dextrose, citric acid, monopotassiumphosphate, and brominated vegetable oil (as a stabilizer), magnesiumchloride, calcium chloride, niacinamide (vitamin B3), vitamin pyridoxinehydrochloride (B6), cyanocobalamin (vitamin B12).

In embodiments, the beverage includes a zero-calorie sweetener. Inembodiments, the beverage includes low-calorie sweetener. Inembodiments, the beverage includes an artificial sweetener. Inembodiments, the beverage includes honey, sugar, aspartame, acesulfamepotassium, saccharin, sucralose, neotame, erythritol, stevia, stevialeaf extract. In embodiments, the beverage includes a sugar alcoholand/or a polyol. In embodiments, the beverage includes electrolytesincluding sodium, potassium, magnesium, calcium. In embodiments, thebeverage includes fruit juice concentrate, citric acid, white teaextract, malic acid, beta carotene, ascorbic acid (vitamin C), sodiumcitrate.

In embodiments, the beverage includes a coloring agent that isconfigured to color the beverage a color that includes one or morecolors selected from the group consisting of: light green (144C), yellow(001A) or yellow green (001A), dark green (144A) with shades of yellow(001A), yellow orange (011A), orange (024A), orange red (033B), orangepink (027A), red (033A), dark purple red (046A), light red pink (039C),red pink (043C), dark pink red (045D), purple red (054A), light bluepink (055C), purple (058A), purple red (059D), blue pink (062A), lightblue violet (069C), violet blue (089A), violet (075A), dark violet(079A), blue violet (083D), blue (100A), dark blue (103A), light blue(104D), light green blue (110C), green blue (111A), grey blue (115C),green blue (125C), white (155A), orange brown (169A), brown (172A),brown purple (178A), orange pink (179D) (The Royal Horticultural SocietyColour Chart, 1995 Ed.).

In embodiments, the water, a biocatalyst, optionally cannabis, and atleast one from the group consisting of malt, grain, barley, honey, andhops may be fermented at a temperature that ranges from one or more fromthe group consisting of 50 degrees Fahrenheit to 52 degrees Fahrenheit,52 degrees Fahrenheit to 54 degrees Fahrenheit, 54 degrees Fahrenheit to56 degrees Fahrenheit, 56 degrees Fahrenheit to 58 degrees Fahrenheit,58 degrees Fahrenheit to 60 degrees Fahrenheit, 60 degrees Fahrenheit to62 degrees Fahrenheit, 62 degrees Fahrenheit to 64 degrees Fahrenheit,64 degrees Fahrenheit to 66 degrees Fahrenheit, 66 degrees Fahrenheit to68 degrees Fahrenheit, 68 degrees Fahrenheit to 70 degrees Fahrenheit,70 degrees Fahrenheit to 72 degrees Fahrenheit, 72 degrees Fahrenheit to74 degrees Fahrenheit, 74 degrees Fahrenheit to 76 degrees Fahrenheit,76 degrees Fahrenheit to 78 degrees Fahrenheit, 78 degrees Fahrenheit to80 degrees Fahrenheit, 80 degrees Fahrenheit to 82 degrees Fahrenheit,82 degrees Fahrenheit to 84 degrees Fahrenheit, 84 degrees Fahrenheit to86 degrees Fahrenheit, 86 degrees Fahrenheit to 88 degrees Fahrenheit,88 degrees Fahrenheit to 90 degrees Fahrenheit, 90 degrees Fahrenheit to92 degrees Fahrenheit, and 92 degrees Fahrenheit to 94 degreesFahrenheit.

In embodiments, the yeast within the mixture of water, yeast, optionallycannabis, and at least one or more from the group consisting of malt,grain, barley, honey, and hops has a range of attenuation that isselected from one or more from the group consisting of 50 percent to 52percent, 52 percent to 54 percent, 54 percent to 56 percent, 56 percentto 58 percent, 58 percent to 60 percent, 60 percent to 62 percent, 62percent to 64 percent, 64 percent to 66 percent, 66 percent to 68percent, 68 percent to 70 percent, 70 percent to 72 percent, 72 percentto 74 percent, 74 percent to 76 percent, 76 percent to 78 percent, 78percent to 80 percent, 80 percent to 82 percent, 82 percent to 84percent, 84 percent to 86 percent, 86 percent to 88 percent, 88 percentto 90 percent, 90 percent to 92 percent, and 92 percent to 94 percent.The term attenuation is a percentage that is used to describe thepercent of sugar within the malt, grain, barley, honey, or hops that isconverted by the yeast into ethanol and carbon dioxide.

The biocatalyst tank (G78) has an interior (G80), a biocatalyst input(G81), a biocatalyst conveyor (G82), and a biocatalyst conveyor output(G83). The biocatalyst tank (G78) accepts biocatalyst (G79) to theinterior (G80) and regulates and controls an engineered amount ofbiocatalyst (G79) downstream to be mixed in the mixing tank (G15). Thebiocatalyst conveyor (G82) has an integrated biocatalyst mass sensor(G84) that is configured to input and output a signal (G85) to thecomputer (COMP). The biocatalyst conveyor motor (G86) has a controller(G87) that is configured to input and output a signal (G88) to thecomputer (COMP). The biocatalyst mass sensor (G84), biocatalyst conveyor(G82), and biocatalyst conveyor motor (G86) are coupled so as to permitthe conveyance, distribution, or output of a precise flow of biocatalyst(G79) via a biocatalyst transfer line (G89). In embodiments, thebiocatalyst transfer line (G89) has a diameter that ranges from: 0.5inches to 0.75 inches, 0.75 inches to 1 inch, 1 inch to 1.5 inches, 2inches to 3 inches, 3 inches to 4 inches.

In embodiments, the biocatalyst includes a SCOBY which is an acronym fora “Symbiotic Culture Of Bacteria and Yeast” which is a syntrophic mixedculture of bacteria and yeast used in production of several traditionalfoods and beverages, such as Kombucha. In embodiments, the beverageincludes Kombucha.

In embodiments, the beverage includes Kombucha which can be stored atroom temperature or without the need for refrigeration. This type ofKombucha has been fermented with a SCOBY and is then filtered to removebacteria and yeast from the beverage, either by pasteurization orfiltration. Kombucha, if it is raw and unpasteurized, contains live,beneficial bacteria and yeast colonies, wherein to increase theshelf-life is it cooked, heated, or pasteurized or filtered to removethe live, beneficial bacteria and yeast colonies to prevent the beveragefrom going bad and spoiling. In embodiments, the beverage isrefrigerated before sale to prevent further fermentation from occurring.In embodiments, the beverage is not refrigerated before sale sincecooking, heating, or pasteurization or filtration takes place.

Acid Distribution Module (14G3′)

FIG. 14G displays an acid mixing module (14G3′) including an acid tank(G78′) that is configured to accept at least one acid (G79′). The acid(G79′) may be comprised of one or more from the group consisting of anacid, abscic acid, acetic acid, ascorbic acid, benzoic acid, citricacid, formic acid, fumaric acid, hydrochloric acid, lactic acid, malicacid, nitric acid, organic acids, phosphoric acid, potassium hydroxide,propionic acid, salicylic acid, sulfamic acid, sulfuric acid, andtartaric acid.

In embodiments, whole insects (G56) and/or ground insects (G67) have apH that is greater than 7. In embodiments, whole insects (G56) and/orground insects (G67) have a pH that is basic and ranges from greaterthan 7 to less than 8.75. In embodiments, whole insects (G56) and/orground insects (G67) added to the interior (G14) of the mixing tank(G15) is required to lower the pH of the water, insect, biocatalystmixture to a pH that is sufficient for the biocatalyst to digest orhydrolyze the insects. In embodiments, addition of an acid (G79′) to theinterior (G14) of the mixing tank (G15) is required to maintain theliquid mixture of biocatalyst, insects, and water within the mixing tank(G15) to be at a desired range from within 6.25 to 7.5.

The acid tank (G78′) has an interior (G80′), an acid input (G81′), anacid conveyor (G82′), and an acid conveyor output (G83′). The acid tank(G78′) accepts acid (G79′) to the interior (G80′) and regulates andcontrols an engineered amount of acid (G79′) downstream to be mixed inthe mixing tank (G15).

The acid conveyor (G82′) has an integrated acid mass sensor (G84′) thatis configured to input and output a signal (G85′) to the computer(COMP). The acid conveyor motor (G86′) has a controller (G87′) that isconfigured to input and output a signal (G88′) to the computer (COMP).The acid mass sensor (G84′), acid conveyor (G82′), and acid conveyormotor (G86′) are coupled so as to permit the conveyance, distribution,or output of a precise flow of acid (G79′) via an acid transfer line(G89′). In embodiments, the acid transfer line (G89′) has a diameterthat ranges from: 0.5 inches to 0.75 inches, 0.75 inches to 1 inch, 1inch to 1.5 inches, 2 inches to 3 inches, 3 inches to 4 inches.

In embodiments, the mixing tank (G15) is equipped with a pH sensor (PHG)that is configured to output a signal (PHG′) to the computer (COMP). Inembodiments, the pH sensor (PHG) is used in a control loop with the acidmass sensor (G84′), acid conveyor (G82′), and acid conveyor motor (G86′)to permit output of a precise flow of acid (G79′) to the interior (G14)of the mixing tank (G15) to maintain a predetermined pH within themixing tank (G15).

FIG. 14G shows the whole insects (G56), ground insects (G67),biocatalyst (G79), and acid (G79′) introduced to the interior (G14) ofthe mixing tank (G15) via an input (G100). It is not required that thewhole insects (G56), ground insects (G67), biocatalyst (G79), and acid(G79′) are combined into a combined stream (G101) for input (G100) tothe interior (G14) of the mixing tank (G15). It is apparent to thoseskilled in the art to which it pertains that each whole insects (G56),ground insects (G67), biocatalyst (G79), and acid (G79′) can have theirown input to the interior (G14) of the mixing tank (G15) as well.

In embodiments, another alternate liquid (G102) may be added to theinterior (G14) of the mixing tank (G15) to replace or be mixed with thesource of water (01). In embodiments, the alternate liquid (G102) arecomprised of one or more from the group consisting of alcohol,diglycerides, esters, ethanol, butanol, n-butanol, sec-butanol,isobutanol, tert-butanol, ethyl acetate, glycerin, glycerol, hexane,hydrocarbon, insect lipids, isopropyl alcohol, methanol, Monoglycerides,oil, and solvent.

In embodiments, at least a portion of the first contaminant depletedwater (G27), second contaminant depleted water (G31), or thirdcontaminant depleted water (G13) may be introduced to thestart-up/shut-down liquid tank (KEA) for use as a source ofstart-up/shut-down water (KEB) as indicated on FIG. 14K. In embodiments,at least a portion of the first contaminant depleted water (G27), secondcontaminant depleted water (G31), or third contaminant depleted water(G13) may be introduced to start-up and/or shut-down the rotary atomizer(KAU) of FIG. 14K and used as start-up/shut-down water (KEB).

FIG. 14H:

FIG. 14H shows one non-limiting embodiment of an exoskeleton separationmodule (14H) that is configured to remove the exoskeleton containedwithin the insect liquid biocatalyst mixture (G09).

FIG. 14H shows the exoskeleton separation module (14H) configured toremove exoskeleton from insects that are contained within the insectliquid biocatalyst mixture (G09). In embodiments, where the biocatalyst(G79) within the biocatalyst mixing module (14G) is optional, theexoskeleton separation module (14H) is configured to remove exoskeletonfrom insects that are contained within an insect and liquid mixture(G09A) as depicted in FIG. 14G. In embodiments, exoskeleton is chitin.In embodiments, exoskeleton is a long-chain polymer of anN-acetylglucosamine, a derivative of glucose. In embodiments, theexoskeleton is provided to the insects to eat within the insect feedingchamber (FC). In embodiments, the exoskeleton removed in the exoskeletonseparation module (14H) is provided to the polymer distribution module(1D) within the enhanced feedstock mixing module (1000) as shown in FIG.2.

The insect liquid biocatalyst mixture (G09) or an insect and liquidmixture (G09A) is transferred from the mixing tank (G15) to theexoskeleton separation module (14H) of FIG. 14H via a transfer conduit(G50). FIG. 14H displays the exoskeleton separation module (14H)including an exoskeleton separator (H10). In embodiments, theexoskeleton separator (H10) is a filter (H11) having at least one sidewall (H65). In embodiments, the filter (H11) is cylindrical. Inembodiments, the filter (H11) is a candle filter (H12) that has at leastone filter element (H13) contained within its interior (H64). Inembodiments, the filter (H11) has a top (H14) and a bottom (H15). FIG.14H shows a separator input (H16) positioned on the side wall (H65) ofthe exoskeleton separator (H10). The separator input (H16) is configuredto introduce an exoskeleton-laden insect mixture (H17) to the interior(H64) of the filter (H11). In embodiments, the insect liquid biocatalystmixture (G09) or an insect and liquid mixture (G09A) may be consideredan exoskeleton-laden insect mixture (H17).

In embodiments, the insects within the mixing tank/bioreactor (G15) ofFIG. 14G are transferred to the filter (H11) on FIG. 14H. Inembodiments, the filter (H11) may is configured to remove solids fromthe insect and liquid mixture (G09A). In embodiments, the filter (H11)is configured to remove a recombinant protein from the insect and liquidmixture (G09A). In embodiments, the filter (H11) is configured to removea the cannabinoid, the biomass (cell walls, microorganisms) includingthe cannabinoid (for use in extraction of the cannabinoid from thebiomass), a recombinant protein, vaccine, antibody, peptide, or chemicalfrom the insect and liquid mixture (G09A).

In embodiments, the bioreactor includes one or more type of bioreactorsselected from the group consisting of a continuous stirred tankbioreactor, a bubble column bioreactor, a microbubble reactor, anairlift bioreactor, a fluidized bed bioreactor, a packed bed bioreactor,a photo-bioreactor, a WAVE Bioreactor™ system from GE Healthcare, andcombinations thereof. Further, photo-bioreactors are well known in theart and are available from a variety of commercial vendors, such asfrom: https://www.alibaba.com, Model Number: HXDYKZ-12, which is aphoto-bioreactor comprising translucent plastic tubes provides asuitable environment for sunlight supply, algae growth and culturedensity; and also, from https://www.alibaba.com, Model Number: SF-100L,which is a photo-bioreactor comprising a jacketed glass reactor; andalso, https://www.ika.com, Algaemaster 10 Control Bioreactor.

In embodiments, the a photo-bioreactor is used is provided with thesource of light, and microorganisms are grown at a Photosynthetic PhotonFlux Density within the photo-bioreactor (in micromole per second andsquare meter (μmol/m2/s)) ranging from 20 to 40, 40 to 50, 50 to 60, 60to 70, 70 to 80, 80 to 90, 90 to 100, 100 to 110, 110 to 120, 120 to130, 130 to 140, 140 to 150, 150 to 160, 160 to 170, 170 to 180, 180 to190, 190 to 200, 200 to 210, 210 to 220, 220 to 230, 230 to 240, 240 to250, 250 to 260, 260 to 270, 270 to 280, 280 to 290, 290 to 300, 300 to400, 400 to 500, 500 to 1,000, 1,000 to 2,000, 2,000 to 5,000. Inembodiments, the microorganisms within the photo-bioreactor are providedwith the source of light, and are grown at a Photosynthetic Photon FluxDensity (in micromole per second and square meter (μmol/m2/s)) rangingfrom 100 to 110 to 130. In embodiments, the Photosynthetic Photon FluxDensity is based on the number of photons in a certain waveband incidentper unit time (s) on a unit area (m2) divided by the Avogadro constant(6.022×1023 mol-1). In embodiments, the photo-bioreactor utilizes alight source to cultivate the microorganisms wherein the microorganismsmay be phototrophic or photosynthetic which use photosynthesis. Inembodiments, phototrophic or photosynthetic genetically modifiedmicroorganisms produce cannabinoids from light within the interior ofthe bioreactor.

In embodiments, the photo-bioreactor grows the cultivatingphotosynthetic genetically modified microorganisms to fix carbon dioxideand produce target products, such as not only including syntheticcannabinoids. This disclosure is aimed at energy-efficient, low cost,photo-bioreactors with carefully designed control systems to monitor theperformance of the microorganisms for large-scale or industrial-scalesynthetic cannabinoid biosynthesis.

In embodiments, the insect cells used within the bioreactor includegenetically modified insect cells. In embodiments, the insect cells usedwithin the bioreactor do not include genetically modified insect cells.In embodiments, the insect cells used within the bioreactor include gasfermenting insect cells. In embodiments, the insect cells used withinthe bioreactor undergo anaerobic respiration. In embodiments, the insectcells used within the bioreactor undergo fermentation. In embodiments,the insect cells used within the bioreactor include anaerobic insectcells. In embodiments, the bioreactor includes a liquid nutrient medium,or culture medium, used for culturing the insect cells and the acannabinoid, recombinant protein, vaccine, antibody, peptide, orchemical is produced within the bioreactor by the insect cells whicheither contain the cannabinoid within the insects and/or insect cells(and later optionally extracted from the insects and/or insect cells) orsecrete the cannabinoid, recombinant protein, vaccine, antibody,peptide, or chemical which accumulates within the liquid nutrientmedium. In embodiments, the chemical includes ethanol. In embodiments,the chemical includes a cannabinoid.

In embodiments, the bioreactor includes a liquid nutrient medium, orculture medium, used for culturing the insect cells and a cannabinoid isproduced within the bioreactor by the insect cells which either containthe cannabinoid within the insects and/or insect cells (and lateroptionally extracted from the insects and/or insect cells) or secretethe cannabinoid which accumulates within the liquid nutrient medium. Inembodiments, the cannabinoid includes tetrahydrocannabinolic acid(THCA), active tetrahydrocannabinol, tetrahydrocannabinol (THC),Δ9-tetrahydrocannabinol Δ9-THC, Δ8-tetrahydrocannabinol Δ8-THC,cannabichromene CBC, cannabidiol CBD, cannabigerol CBG, cannabinidiolCBND, and/or cannabinol CBN. In embodiments, the bioreactor includes aliquid nutrient medium, or culture medium, used for culturing the insectcells and terpenes is produced within the bioreactor by the insect cellswhich either contain the cannabinoid within the insects and/or insectcells (and later optionally extracted from the insects and/or insectcells) or secrete the terpenes which accumulate within the liquidnutrient medium, wherein the terpenes include one or more from the groupconsisting of limonene, humulene, pinene, linalool, caryophyllene,myrcene, eucalyptol, nerolidol, bisablol, and phytol.

Methods for producing a partially biosynthetic cannabinoid distillate isdescribed. The method includes mixing partially biosyntheticcannabinoids with plant derived cannabinoids to produce a cannabinoiddistillate that includes both plant-derived cannabinoids together withpartially biosynthetic cannabinoids. Methods to produce the biosyntheticcannabinoid are described and include use of a bioreactor including aliquid nutrient medium, or culture medium, used for culturinggenetically modified microorganisms and a cannabinoid is produced withinthe bioreactor by the genetically modified microorganisms which eithercontain the cannabinoid within the cells of the microorganisms (andlater extracted from the microorganisms) or secrete the cannabinoidwhich accumulates within the liquid nutrient medium. Purification andextraction of the cannabinoids from the genetically modifiedmicroorganisms then takes place to produce a source of biosyntheticcannabinoid distillate which is then mixed with plant-derivedcannabinoids to produce a cannabinoid distillate that includes bothplant-derived cannabinoids together with partially biosyntheticcannabinoids.

In embodiments, the bioreactor is provided with a gas, including air orcarbon dioxide. In embodiment, the carbon dioxide concentration of thegas introduced to the bioreactor ranges from 400 to 30,000 parts permillion. In embodiment, the carbon dioxide is recycled from the carbondioxide recovery system s disclosed in FIG. 17F′.

In embodiments, the bioreactor includes a liquid nutrient medium, orculture medium, used for culturing genetically modified microorganismsand a cannabinoid is produced within the bioreactor by the geneticallymodified microorganisms which either contain the cannabinoid within thecells of the microorganisms (and later extracted from themicroorganisms) or secrete the cannabinoid which accumulates within theliquid nutrient medium. In embodiments, the cannabinoid includestetrahydrocannabinolic acid (THCA), active tetrahydrocannabinol,tetrahydrocannabinol (THC), Δ9-tetrahydrocannabinol Δ9-THC,Δ8-tetrahydrocannabinol Δ8-THC, cannabichromene CBC, cannabidiol CBD,cannabigerol CBG, cannabinidiol CBND, and/or cannabinol CBN. Inembodiments, the bioreactor includes a liquid nutrient medium, orculture medium, used for culturing the microorganisms and terpenes isproduced within the bioreactor by the microorganisms which eithercontain the terpenes within the cells of the microorganisms (and laterextracted from the microorganisms) secrete the terpenes which accumulatewithin the liquid nutrient medium, wherein the terpenes include one ormore from the group consisting of limonene, humulene, pinene, linalool,caryophyllene, myrcene, eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the bioreactor (G15) includes a liquid nutrient medium,or culture medium, used for culturing microorganisms includinggenetically modified algae and a cannabinoid is produced within thebioreactor by the genetically modified algae which either contain thecannabinoid within the cells of the microorganisms (and later extractedfrom the microorganisms) or secrete the cannabinoid which accumulateswithin the liquid nutrient medium. In embodiments, the cannabinoidincludes tetrahydrocannabinolic acid (THCA), activetetrahydrocannabinol, tetrahydrocannabinol (THC),Δ9-tetrahydrocannabinol Δ9-THC, Δ8-tetrahydrocannabinol Δ8-THC,cannabichromene CBC, cannabidiol CBD, cannabigerol CBG, cannabinidiolCBND, and/or cannabinol CBN. In embodiments, the bioreactor includes aliquid nutrient medium, or culture medium, used for culturing thegenetically modified algae and terpenes is produced within thebioreactor by the genetically modified algae which either contain theterpenes within the cells of the genetically modified algae (and laterextracted from the microorganisms) or secrete the terpenes whichaccumulate within the liquid nutrient medium, wherein the terpenesinclude one or more from the group consisting of limonene, humulene,pinene, linalool, caryophyllene, myrcene, eucalyptol, nerolidol,bisablol, and phytol.

In embodiments, the microorganisms used within the bioreactor (G15)include bacteria, archaea, fungi, protozoa, algae, and viruses. Inembodiments, the microorganisms used within the bioreactor includegenetically modified photosynthetic microalgae or a cyanobacterium. Inembodiments, the microorganisms used within the bioreactor includegenetically modified organisms. In embodiments, the microorganisms usedwithin the bioreactor include genetically modified algae. Inembodiments, the microorganisms used within the bioreactor do notinclude genetically modified organisms. In embodiments, themicroorganisms used within the bioreactor include gas fermentingorganisms. In embodiments, the microorganisms used within the bioreactorundergo anaerobic respiration. In embodiments, the microorganisms usedwithin the bioreactor undergo fermentation. In embodiments, themicroorganisms used within the bioreactor include anaerobic bacteria.

In embodiments, the microorganisms used within the bioreactor (G15)include genetically modified algae. In embodiments, the geneticallymodified algae include cloned algae cells. In embodiments, thegenetically modified algae includes one or more selected from the groupconsisting of: polyclonal genetically modified algae cells, polyclonalgenetically modified algae cells infected with a virus, polyclonalgenetically modified algae cells infected with a recombinant virus,polyclonal genetically modified algae cells infected with a polyclonalrecombinant virus, polyclonal genetically modified algae cells infectedwith an oligoclonal recombinant virus, polyclonal genetically modifiedalgae cells infected with a monoclonal recombinant virus, andcombinations thereof.

In embodiments, the genetically modified algae includes one or moreselected from the group consisting of: oligoclonal genetically modifiedalgae cells, oligoclonal genetically modified algae cells infected witha virus, oligoclonal genetically modified algae cells infected with arecombinant virus, oligoclonal genetically modified algae cells infectedwith a polyclonal recombinant virus, oligoclonal genetically modifiedalgae cells infected with an oligoclonal recombinant virus, oligoclonalgenetically modified algae cells infected with a monoclonal recombinantvirus, and combinations thereof.

In embodiments, the genetically modified algae includes one or moreselected from the group consisting of: monoclonal genetically modifiedalgae cells, monoclonal genetically modified algae cells infected with avirus, monoclonal genetically modified algae cells infected with arecombinant virus, monoclonal genetically modified algae cells infectedwith a polyclonal recombinant virus, monoclonal genetically modifiedalgae cells infected with an oligoclonal recombinant virus, monoclonalgenetically modified algae cells infected with a monoclonal recombinantvirus, and combinations thereof.

In embodiments, the microorganisms used within the bioreactor includegenetically modified cyanobacterium. In embodiments, the geneticallymodified cyanobacterium include cloned cyanobacterium cells. Inembodiments, the genetically modified cyanobacterium includes one ormore selected from the group consisting of: polyclonal geneticallymodified cyanobacterium cells, polyclonal genetically modifiedcyanobacterium cells infected with a virus, polyclonal geneticallymodified cyanobacterium cells infected with a recombinant virus,polyclonal genetically modified cyanobacterium cells infected with apolyclonal recombinant virus, polyclonal genetically modifiedcyanobacterium cells infected with an oligoclonal recombinant virus,polyclonal genetically modified cyanobacterium cells infected with amonoclonal recombinant virus, and combinations thereof.

In embodiments, the genetically modified cyanobacterium includes one ormore selected from the group consisting of: oligoclonal geneticallymodified cyanobacterium cells, oligoclonal genetically modifiedcyanobacterium cells infected with a virus, oligoclonal geneticallymodified cyanobacterium cells infected with a recombinant virus,oligoclonal genetically modified cyanobacterium cells infected with apolyclonal recombinant virus, oligoclonal genetically modifiedcyanobacterium cells infected with an oligoclonal recombinant virus,oligoclonal genetically modified cyanobacterium cells infected with amonoclonal recombinant virus, and combinations thereof.

In embodiments, the genetically modified cyanobacterium includes one ormore selected from the group consisting of: monoclonal geneticallymodified cyanobacterium cells, monoclonal genetically modifiedcyanobacterium cells infected with a virus, monoclonal geneticallymodified cyanobacterium cells infected with a recombinant virus,monoclonal genetically modified cyanobacterium cells infected with apolyclonal recombinant virus, monoclonal genetically modifiedcyanobacterium cells infected with an oligoclonal recombinant virus,monoclonal genetically modified cyanobacterium cells infected with amonoclonal recombinant virus, and combinations thereof.

In embodiments, the bioreactor (G15) includes a single-use bioreactor.In embodiments, the single-use bioreactor includes a disposablebioreactor. In embodiments, the disposable bioreactor is a disposablebag instead of a culture vessel. In embodiments, the disposablebioreactor is a disposable bag. In embodiments, the bioreactor (G15) istransparent or translucent.

In embodiments, the disposable bag includes a three-layer plastic foil,comprising: a first layer including a first polymer configured toprovide mechanical stability, wherein the first polymer includespolyethylene terephthalate or low-density polyethylene (LDPE); a secondlayer including a second polymer configured to act as a gas barrier,wherein the second polymer includes a first thermoplastic polymer,wherein the first thermoplastic polymer includes an aliphatic rubberysynthetic polymer, a material of the polyvinyl ester family, polyvinylchloride, polyvinyl, or vinyl; and a third layer including a thirdpolymer configured to contact the liquid within the bioreactor, whereinthe liquid includes a culture medium including at least treated water,wherein the third polymer includes a second thermoplastic polymer,wherein the second thermoplastic polymer includes an aliphatic rubberysynthetic polymer, a material of the polyvinyl ester family, polyvinylacetate (PVA, PVAc, poly(ethenyl ethanoate), polypropylene, orpolypropene.

In embodiments, the liquid or culture medium within the disposablebioreactor is agitated. In embodiments, the disposable bioreactorincludes a stirrer within bag to agitate the culture medium or liquidwithin the bioreactor. In embodiments, the stirrer is integrated intothe disposable bag. In embodiments, the disposable bioreactor ispre-sterilized. In embodiments, the liquid or culture medium within thedisposable bioreactor is agitated by a rocking motion. In embodiments,the liquid or culture medium within the disposable bioreactor is notagitated. In embodiments, the disposable bioreactor includes a stirrerwithin bag to agitate the culture medium. In embodiments, the disposablebioreactor reduces risk of cross-contamination between batches whileproviding flexibility, minimizing turnaround time, reducing cleaningcosts, and easing validation restrictions.

In embodiments, the bioreactor (G15) provides scalable and robuststirred-tank or disposable performance in both cGMP and non-cGMPenvironments. In embodiments, the bioreactor (G15) includes a volume, inliters, ranging from 1, 5, 10, 50, 200, 500, 1000, or 2000. Inembodiments, the bioreactor (G15) includes a perfusion bioreactor. Inembodiments, the bioreactor (G15) is configured to operate in aplurality of modes, including: batch, fed-batch and perfusion bioreactormodes.

In embodiments, the filter (H11) includes one or more filter typesselected from the group consisting of: a batch filter, a continuousfilter, a continuous-batch filter, a leaf filter, a filter press, acentrifuge, a plate and frame filter, a recessed filter plate, amembrane filter press, a disc filter, a centrifugal filter, ahydroclone, an s-type filter belt press, a klampress belt press, a beltpress, a basket filter, a chromatography column, a packed column, apacked bed, a chromatography filtration, adsorber, absorber, a membrane,ion exchange resin. In embodiments, the filter (H11) includes one ormore filter types selected from the group consisting of microfiltration,depth filtration, ultrafiltration, diafiltration, tangential flowfiltration (TFF) system, sterile filtration, and rotary vacuum drumfiltration. In embodiments, the filter (H44) includes a General ElectricAKTA liquid chromatography system.

In embodiments, the filter (H11) includes an adsorbent comprising one ormore selected from the group consisting of a strongly acidic cationexchange resin include such as AMBERLITE IR-118 (Available from DowChemical Company, Midland, Mich.), or DIAION PK216LH (Available fromMitsubishi Chemical Company, Tokyo, Japan). Suitable examples of theweakly basic anion exchange resin include AMBERLITE IRA-70RF (Availablefrom Dow Chemical Company, Midland, Mich.) or RELITE RAM2 (Availablefrom Mitsubishi Chemical Company, Tokyo, Japan).

In embodiments, the adsorbent used in the filter (H11) employed is acombination of styrene-divinyl benzene copolymer, ion exchange andhydrophobic interaction based stationary phase adsorbents and a mobilephase comprising water in a combination of normal and reverse phasesimulated moving bed separation zones to provide a first purifiedrecombinant protein.

In embodiments, the filter (H11) includes one or more filters orpurification systems selected from the group consisting of affinitychromatography (AC), ion exchange chromatography (IEX), hydrophobicinteraction chromatography (HIC), gel filtration (GF) chromatography,reversed phase chromatography (RPC), and combinations thereof.

In embodiments, the filter (H11) includes a detergent purificationsystem, wherein the detergent includes a surfactant, ionic detergent,non-ionic detergent, and/or a zwitterionic detergent. In embodiments,the filter (H11) includes a detergent purification system, wherein thedetergent includes one or more detergents selected from the groupconsisting of a surfactant, a nonionic surfactant, lecithin,polyethylene (40), stearate, polysorbate, Polyoxyethylene sorbitanmonooleate, Polyoxyethylene (20) sorbitan monooleate, polysorbate 80,polysorbate 60, polysorbate 65, ammonium salts of phosphatidic acid,sucrose acetate isobutyrate, potassium pyrophosphate, sodium acidpyrophosphate, sodium pyrophosphate, potassium polymetaphosphate, sodiummetaphosphate, insoluble or sodium polyphosphates, sodiumpolyphosphates, insoluble polyphosphates, glassy salts of fatty acids,mono- and di-glycerides of fatty acids, mono-glycerides of fatty acids,di-glycerides of fatty acids, acetic and fatty acid esters of glycerol,lactic and fatty acid esters of glycerol, citric and fatty acid estersof glycerol, diacetyltartaric and fatty acid esters of glycerol, mixedfatty acid esters of glycerol, sucrose esters of fatty acids,polyglycerol esters of fatty acids, polyglycerol esters ofinteresterified ricinoleic acid, propylene glycol mono- and di-esters,propylene glycol di-esters, propylene glycol mono-esters, propyleneglycol esters of fatty acids, propylene glycol esters, dioctyl sodiumsulphosuccinate, sodium lactylate, sodium oleyl lactylate, sodiumstearoyl lactylate, calcium lactylate, calcium oleyl lactylate, calciumstearoyl lactylate, sorbitan monostearate, maltodextrin, polyphosphates,formulated polyphosphates, and gum arabic.

In embodiments, the biocatalyst (G79) and acid (G79′) within the mixingtank (G15) hydrolyzes chitosan. In embodiments, the biocatalyst (G79)and acid (G79′) hydrolyze the chitosan within the mixing tank (G15). Inembodiments, the biocatalyst (G79) and acid (G79′) hydrolyzedeacetylated insects (1570″) within the mixing tank (G15). Inembodiments, the biocatalyst (G79) and acid (G79′) hydrolyze thebiopolymer (1570′) within the mixing tank (G15).

In embodiments, introducing biocatalyst (G79), acid (G79′), anddeacetylated insects (1570″) to the mixing tank (G15) hydrolyzes thedeacetylated insects (1570″) to produce an oligosaccharide (G09′). Inembodiments, introducing biocatalyst (G79), acid (G79′), and biopolymer(1570′) to the mixing tank (G15) hydrolyzes the biopolymer (1570′) toproduce a hydrolyzed-biopolymer (G09″) containing at least anoligosaccharide (G09′). In embodiments, introducing the biocatalyst(G79), acid (G79′), and insects (G07), that include deacetylated insects(1570″), to the mixing tank (G15) hydrolyzes the deacetylated insects(1570″) to produce an oligosaccharide (G09′). In embodiments,introducing the biocatalyst (G79), acid (G79′), and insects (G07) thatinclude deacetylated insects (1570″) to the mixing tank (G15) hydrolyzesthe deacetylated insects (1570″) to produce a hydrolyzed-biopolymer(G09″). In embodiments, the insect liquid biocatalyst mixture (G09)includes an oligosaccharide (G09′). In embodiments, the insect liquidbiocatalyst mixture (G09) includes a hydrolyzed-biopolymer (G09″).

A supply valve (H61) equipped with a controller (H62) and configured toinput and output a signal (H63) to the computer (COMP) is positioned onthe transfer conduit (G50) in between the mixing tank (G15) of FIG. 14Gand the separator input (H16) positioned on the side wall (H65) of theexoskeleton separator (H10).

The filter (H11) has a first output (H18) positioned on the top (H14).The first output (H18) is configured to discharge anexoskeleton-depleted insect liquid mixture (H19) via anexoskeleton-depleted mixture conduit (H20). A discharge valve (H21)equipped with a controller (H22) and configured to input and output asignal (H23) to the computer (COMP) is positioned on theexoskeleton-depleted mixture conduit (H20). The filter (H11) isconfigured to remove exoskeleton (H46) from either the insect liquidbiocatalyst mixture (G09) or the insect and liquid mixture (G09A) toform an exoskeleton-depleted insect liquid mixture (H19). Theexoskeleton-depleted insect liquid mixture (H19) has a reduced amount ofexoskeleton (H46) relative to the insect liquid biocatalyst mixture(G09) or an insect and liquid mixture (G09A).

In embodiments, a flow sensor (H24) and a secondary filter (H25) areboth installed on the exoskeleton-depleted mixture conduit (H20). Theflow sensor (H24) can be an electronic instrument, but a manualpaddle-wheel type flow sensor or a totalizer are preferred. Alternately,the flow sensor (H24) may be of a rotameter, variable-area flow meter, abullseye type flow sensor, or a sight-glass type sensor and configuredto allow one to visually observe the clarity, and lack of exoskeletonsolids within the exoskeleton-depleted insect liquid mixture (H19). Thesecondary filter (H25) is used as an emergency filter to preventcontamination of the downstream exoskeleton-depleted insect liquidmixture tank (H26). In embodiments, the exoskeleton-depleted insectliquid mixture tank (H26) is synonymous with an insect liquid mixturetank (H26).

In embodiments, a centrifuge (H11) is configured to remove a recombinantprotein from the insect and liquid mixture (G09A). In embodiments, acentrifugal filter (H11) is configured to remove a recombinant proteinfrom the insect and liquid mixture (G09A). In embodiments, therecombinant protein separated from the insect and liquid mixture (G09A)is then purified. In embodiments, the recombinant protein separated fromthe insect and liquid mixture (G09A) is transferred to the insect liquidmixture tank (H26).

The secondary filter (H25) is preferably installed to mitigate any riskof contamination downstream in the event that the filter element (H13)becomes ruptured and solid exoskeleton particles are transferred via theexoskeleton-depleted mixture conduit (H20) and into the interior (H27)of the exoskeleton-depleted insect liquid mixture tank (H26).

An exoskeleton-depleted insect liquid mixture tank (H26) is connected tothe exoskeleton-depleted mixture conduit (H20) and configured to receivethe exoskeleton-depleted insect liquid mixture (H19) from theexoskeleton separator (H10). The exoskeleton-depleted mixture conduit(H20) is connected at one end to the first output (H18) of theexoskeleton separator (H10) and at another end to the input (H28) of theexoskeleton-depleted insect liquid mixture tank (H26).

The exoskeleton-depleted insect liquid mixture tank (H26) has an input(H28) through which an exoskeleton-depleted insect liquid mixture (H19)is received to the interior (H27). A diptube (H29) may be installed onthe input (H28) of the exoskeleton-depleted insect liquid mixture tank(H26) to introduce the exoskeleton-depleted insect liquid mixture (H19)to the interior (H27) beneath the liquid level. An upper level sensor(H30) and lower level sensor (H31) are installed on theexoskeleton-depleted insect liquid mixture tank (H26). A mixer (H32)with a motor (H33) may also be installed on the exoskeleton-depletedinsect liquid mixture tank (H26) to provide agitation of the liquidcontents within the interior (H27). A heat exchanger (H34) may beinstalled to heat a portion of the exoskeleton-depleted insect liquidmixture (H19) within the exoskeleton-depleted insect liquid mixture tank(H26). A temperature sensor (H35) may be installed on theexoskeleton-depleted insect liquid mixture tank (H26). A mass sensor(H36) may be installed on the exoskeleton-depleted insect liquid mixturetank (H26). In embodiments, a sixth steam supply (LDF) is made availableto the heat exchanger (H34) to heat the liquid slurry within theinterior (H27) of the exoskeleton-depleted insect liquid mixture tank(H26). In embodiments, the heat exchanger (H34) discharges a sixthcondensate (LAV) to the condensate tank (LAP) that is shown on FIG. 14L.

The exoskeleton-depleted insect liquid mixture tank (H26) has an output(H37) that is configured to discharge an exoskeleton-depleted insectliquid mixture (H39) from the interior (H27). An exoskeleton-depletedinsect liquid mixture conduit (H38) is connected to the output (H37) andconfigured to transfer exoskeleton-depleted insect liquid mixture (H39)away from the interior (H27) and towards the liquid separation module(LSM) shown in FIGS. 14i and 14J.

A pump (H40) is interposed on the exoskeleton-depleted insect liquidmixture conduit (H38) and configured to pressurize theexoskeleton-depleted insect liquid mixture (H39) to form a pressurizedexoskeleton-depleted insect liquid mixture (H41). A pressure sensor(H42) is installed on the exoskeleton-depleted insect liquid mixtureconduit (H38). In embodiments, the pump (H40) is configured topressurize the exoskeleton-depleted insect liquid mixture (H39) to apressure that ranges from between 10 pounds per square inch (PSI) to 20PSI; 20 PSI to 30 PSI; 30 PSI to 40 PSI; 40 PSI to 50 PSI; 50 PSI to 60PSI; 60 PSI to 70 PSI; 70 PSI to 80 PSI; 80 PSI to 90 PSI; 90 PSI to 100PSI; 100 PSI to 125 PSI; 125 PSI to 150 PSI; 150 PSI to 200 PSI; 200 PSIto 300 PSI; 300 PSI to 500 PSI.

A recirculation conduit (H43) may be positioned on theexoskeleton-depleted insect liquid mixture conduit (H38) and configuredto transport a portion of the pressurized exoskeleton-depleted insectliquid mixture (H41) back to the interior (H27) of theexoskeleton-depleted insect liquid mixture tank (H26). A filter (H44)may be positioned on the recirculation conduit (H43) to remove anyparticulates from the pressurized exoskeleton-depleted insect liquidmixture (H41) before being sent back to the interior (H27) of theexoskeleton-depleted insect liquid mixture tank (H26). A filter (H44)may be positioned on the recirculation conduit (H43) to purify therecombinant protein from the pressurized exoskeleton-depleted insectliquid mixture (H41) before being sent back to the interior (H27) of theexoskeleton-depleted insect liquid mixture tank (H26). In embodiments,the filter (H44) includes a protein purification system.

In embodiments, the recombinant protein separated from the insect andliquid mixture (G09A) is transferred from the insect liquid mixture tank(H26) to the filter (H44). In embodiments, the filter (H44) includes oneor more filter types selected from the group consisting of: a batchfilter, a continuous filter, a continuous-batch filter, a leaf filter, afilter press, a centrifuge, a plate and frame filter, a recessed filterplate, a membrane filter press, a disc filter, a centrifugal filter, ahydroclone, an s-type filter belt press, a klampress belt press, a beltpress, a basket filter, a chromatography column, a packed column, apacked bed, a chromatography filtration, adsorber, a membrane, absorber,ion exchange resin. In embodiments, the filter (H44) includes one ormore filter types selected from the group consisting of microfiltration,depth filtration, ultrafiltration, diafiltration, tangential flowfiltration (TFF) system, sterile filtration, and rotary vacuum drumfiltration. In embodiments, the filter (H44) includes a General ElectricAKTA liquid chromatography system.

In embodiments, the filter (H44) includes an adsorbent comprising one ormore selected from the group consisting of a strongly acidic cationexchange resin include such as AMBERLITE IR-118 (Available from DowChemical Company, Midland, Mich.), or DIAION PK216LH (Available fromMitsubishi Chemical Company, Tokyo, Japan). Suitable examples of theweakly basic anion exchange resin include AMBERLITE IRA-70RF (Availablefrom Dow Chemical Company, Midland, Mich.) or RELITE RAM2 (Availablefrom Mitsubishi Chemical Company, Tokyo, Japan).

In embodiments, the adsorbent used in the filter (H44) employed is acombination of styrene-divinyl benzene copolymer, ion exchange andhydrophobic interaction based stationary phase adsorbents and a mobilephase comprising water in a combination of normal and reverse phasesimulated moving bed separation zones to provide a second purifiedrecombinant protein.

In embodiments, the filter (H44) includes one or more purificationsystems selected from the group consisting of affinity chromatography(AC), ion exchange chromatography (IEX), hydrophobic interactionchromatography (HIC), gel filtration (GF) chromatography, reversed phasechromatography (RPC), and combinations thereof.

In embodiments, the filter (H44) includes a detergent purificationsystem, wherein the detergent includes a surfactant, ionic detergent,non-ionic detergent, and/or a zwitterionic detergent. In embodiments,the filter (H44) includes a detergent purification system, wherein thedetergent includes one or more detergents selected from the groupconsisting of a surfactant, a nonionic surfactant, lecithin,polyethylene (40), stearate, polysorbate, Polyoxyethylene sorbitanmonooleate, Polyoxyethylene (20) sorbitan monooleate, polysorbate 80,polysorbate 60, polysorbate 65, ammonium salts of phosphatidic acid,sucrose acetate isobutyrate, potassium pyrophosphate, sodium acidpyrophosphate, sodium pyrophosphate, potassium polymetaphosphate, sodiummetaphosphate, insoluble or sodium polyphosphates, sodiumpolyphosphates, insoluble polyphosphates, glassy salts of fatty acids,mono- and di-glycerides of fatty acids, mono-glycerides of fatty acids,di-glycerides of fatty acids, acetic and fatty acid esters of glycerol,lactic and fatty acid esters of glycerol, citric and fatty acid estersof glycerol, diacetyltartaric and fatty acid esters of glycerol, mixedfatty acid esters of glycerol, sucrose esters of fatty acids,polyglycerol esters of fatty acids, polyglycerol esters ofinteresterified ricinoleic acid, propylene glycol mono- and di-esters,propylene glycol di-esters, propylene glycol mono-esters, propyleneglycol esters of fatty acids, propylene glycol esters, dioctyl sodiumsulphosuccinate, sodium lactylate, sodium oleyl lactylate, sodiumstearoyl lactylate, calcium lactylate, calcium oleyl lactylate, calciumstearoyl lactylate, sorbitan monostearate, maltodextrin, polyphosphates,formulated polyphosphates, and gum arabic.

The filter (H11) has a second output (H45) positioned on the bottom(H15). Exoskeleton (H46) may be separated from the insect liquidbiocatalyst mixture (G09) or an insect and liquid mixture (G09A). Aseparated exoskeleton transfer conduit (H47) is connected to the secondoutput (H45) positioned on the bottom (H15) of the filter (H11). Anexoskeleton conveyor (H48) is equipped to receive exoskeleton (H46) fromthe separated exoskeleton transfer conduit (H47).

An exoskeleton drying gas (H49) may be applied to a portion of theexoskeleton (H46) to remove liquid therefrom and form dehydratedexoskeleton (H50). In embodiments, the exoskeleton drying gas (H49) isheated to a temperature ranging from between 80 degrees F. to 90 degreesF.; 90 degrees F. to 100 degrees F.; 100 degrees F. to 110 degrees F.;110 degrees F. to 120 degrees F.; 120 degrees F. to 140 degrees F.; 140degrees F. to 160 degrees F.; 160 degrees F. to 180 degrees F.; 180degrees F. to 200 degrees F.; 200 degrees F. to 250 degrees F.; 250degrees F. to 300 degrees F.; 300 degrees F. to 400 degrees F.

An exoskeleton discharge valve (H51) equipped with a controller (H52)and configured to input and output a signal (H53) to the computer (COMP)is installed on the separated exoskeleton transfer conduit (H47).

A backflush fluid (H54) may be provided to the filter (H11) toregenerate the filter element (H13). FIG. 14H shows the backflush fluid(H54) entering the exoskeleton-depleted mixture conduit (H20) and thenentering the interior (H64) of the filter (H11) via the first output(H18). In embodiments, the backflush fluid (H54) is a liquid. Inembodiments, the backflush fluid (H54) is a gas.

A backflush fluid transfer conduit (H55) is connected to theexoskeleton-depleted mixture conduit (H20) via a connection (H70) inbetween the discharge valve (H21) and the first output (H18). Abackflush fluid supply valve (H56) equipped with a controller (H57) andconfigured to input and output a signal (H58) to the computer (COMP) ispositioned on the backflush fluid transfer conduit (H55). Inembodiments, a backflush fluid pressure regulating valve (H59) with abackflush pressure sensor (H60) is positioned upstream of the backflushfluid supply valve (H56). In embodiments, the backflush fluid pressureregulating valve (H59) may be adjusted to a pressure that is less thanthe rupture pressure of that of the filter element (H13). It ispreferred to counter currently backflush the filter element (H13) bysetting the pressure of the backflush fluid pressure regulating valve(H59) to a pressure of 0.25 PSI to 0.5 PSI; 0.5 PSI to 1.5 PSI; 1.5 PSIto 3 PSI; 3 PSI to 6 PSI; 6 PSI to 9 PSI; 9 PSI to 15 PSI.

The best mode of operation for realizing a continuous filtrate streamdepleted of exoskeleton and encompasses operating the filtration systemin a manner which allows for periodic back flushing of the filterelement cloth surface in-situ by providing a counter-current flow ofbackflush fluid to the filter element. The backwashing dislodges anyaccumulated exoskeleton, in the form of a filter cake, allowing it tosink to the bottom of the filter for removal of the system as a thick,paste-like, filter cake substance.

It is preferred to utilize differential pressure across a filter bundleas the main variable to determine when to undergo a back-flushing cycle,as opposed to using manual predetermined periodic time durationintervals, or using the reduction in flow through the filter bundles asthe variable dictating when to commence filter back flushing,(synonymously termed ‘filter cleaning’, or ‘filter backwashing’,‘in-situ filter cleaning’, or ‘filter surface in-situ regeneration’).Filter element differential pressure between 0.25 and 15 PSI iscommensurate with preferable cake thickness of 20 to 35 millimeters. Incontrast, using manual predetermined periodic time duration intervals asthe sole mechanism to determine when to commence filter cleaning, oftenresults in operational impairment, in that ‘cake bridging’ more readilyoccurs. ‘Cake bridging’ may be described as a large mass of agglomeratedexoskeleton suspended solids filling the spaces between the filterelements and thus posing a challenge to regenerate in-situ, frequentlyrequiring process interruption for physical cleaning and removal of theheavy, gelatinous exoskeleton filter cake.

In-situ filter cleaning may be accomplished by reversing the flow ofliquid or gas through the filter element thereby dislodging exoskeletonfilter cake from the cloth surface thus allowing it to sink to thebottom of the interior of the filter. This affords operations the luxuryof minimizing losses of valuable solvent while draining the filter cakefrom the system.

Filter Operating Procedure

Herein is described the preferred operating procedure for continuousfiltration of exoskeleton. Filtration [step 950] cooperates with thecyclic-batch filter in-situ cleaning steps of: filter element [step952]; filter backflush [step 954]; filter cake sedimentation [step 956];filter cake discharge start [step 958]; filter cake discharge end [step960]; and filtration restart preparation [step 962].

In step 950, (filtration), filtration proceeds and the filter pressuredrop is monitored. As a filtration cycle progresses, solid exoskeletonparticles are deposited onto the surface of the filter element andadhere to its surface until a nominal target differential pressure dropbetween around 0.25 to 15 PSI is attained, which is proportionate to apredetermined thickness of 20 to 35 millimeters. If the filter pressuredrop is lower than the nominal target differential pressure drop, thefiltering cycle continues until the nominal target differential pressuredrop is reached. When a filter has reached its nominal targetdifferential pressure drop, a filter cleaning cycle will commence, whichbegins with step 952 (filter bundle isolation). The sequential stepsencompassing filtration and filter cleaning can be further illuminatedby using FIG. 14H, which visually indicate some of the valve sequencinginvolved, as indicated by open and closed valve positions, illustratedby ‘non-darkened-in valves’ and ‘darkened-in valves’, respectively,wherein: supply valve (H61) is open; discharge valve (H21) is open;backflush fluid supply valve (H56) is closed; exoskeleton dischargevalve (H51) is closed.

When a nominal target pressure drop across a filter is attained, theexoskeleton filter cake material must be dislodged from the filterelement, and thus step 952 (filter isolation) proceeds, which involvesisolating the filter by closing the supply valve (H61) and dischargevalve.

Once both the supply valve (H61) and discharge valve are closed, toisolate the filter, step 954 may proceed. Step 954, (filtratebackflush), involves transferring a backflush fluid (liquid or gas) tobackflush the filter. In embodiments, a typical backflush, in step 954,requires that the backflush fluid supply valve (H56) need be left openfor a duration between: 5 seconds to 10 seconds; 10 seconds to 30seconds; 30 seconds to 1 minute; 1 minute to 5 minutes; 5 minutes to 15minutes; 15 minutes to 30 minutes; 30 minutes to 60 minutes; 60 minutesto 90 minutes.

After the backflush fluid (H54) has been introduced to the filter, andonce the backflush fluid supply valve (H56) has been returned to aclosed position, step 956 may commence. Step 956 (exoskeleton filtercake sedimentation) entails allowing the dislodged exoskeleton filtercake solids to sink to the bottom of the filter.

Step 958 (exoskeleton filter cake discharge start) involves opening theexoskeleton discharge valve (H51) to allow transference of anagglomerated exoskeleton particulate filter cake material from thesystem. The backflush fluid (H54) may be liquid or gas or a combinationof both during Step 958. In embodiments, a gas may be used to dry theexoskeleton and then dislodge the dried exoskeleton from the surface ofthe filter element (H13).

Step 960 (filter cake discharge end) entails closing the exoskeletondischarge valve (H51) since exoskeleton have been discharged from thesystem. After step 960 has transpired, step 962 (filtration restartpreparation) may commence which entails opening the supply valve (H61)and discharge valve (H21) to again commence filtration on theregenerated filter bundle, thus allowing step 950 to commence again,then allowing the filtration and regeneration cycle to repeat itself.

In embodiments, the pharmaceutical composition includes a cannabinoid,recombinant protein, vaccine, antibody, peptide, or chemical, or lectin.In embodiments, the pharmaceutical composition is derived from: arecombinant baculovirus. In embodiments, the virus includes a polyclonalrecombinant baculovirus; and the recombinant baculovirus includes agenetically modified baculovirus where a foreign gene is inserted intoto produce a protein. In embodiments, the pharmaceutical compositionincludes a protein produced from the recombinant baculovirus includes acannabinoid, recombinant protein, vaccine, antibody, peptide, orchemical.

In embodiments, the pharmaceutical composition is derived from: clonedinsect cells; polyclonal insect cells; polyclonal insect cells infectedwith a baculovirus; polyclonal insect cells infected with a recombinantbaculovirus; polyclonal insect cells infected with a polyclonalrecombinant baculovirus; polyclonal insect cells infected with anoligoclonal recombinant baculovirus; polyclonal insect cells infectedwith a monoclonal recombinant baculovirus; oligoclonal insect cells;oligoclonal insect cells infected with a baculovirus; oligoclonal insectcells infected with a recombinant baculovirus; oligoclonal insect cellsinfected with a polyclonal recombinant baculovirus; oligoclonal insectcells infected with an oligoclonal recombinant baculovirus; oligoclonalinsect cells infected with a monoclonal recombinant baculovirus;monoclonal insect cells; monoclonal insect cells infected with abaculovirus; monoclonal insect cells infected with a recombinantbaculovirus; monoclonal insect cells infected with a polyclonalrecombinant baculovirus; monoclonal insect cells infected with anoligoclonal recombinant baculovirus; and/or monoclonal insect cellsinfected with a monoclonal recombinant baculovirus.

In embodiments, the pharmaceutical composition is derived from:genetically modified microorganisms, algae, cloned insects; transgenicinsects; genetically engineered insects; insects that are infected witha recombinant baculovirus; insects that are infected with a clonedrecombinant baculovirus; insects that are infected with a polyclonalrecombinant baculovirus; insects that are infected with an oligoclonalrecombinant baculovirus; and/or insects that are infected with amonoclonal recombinant baculovirus.

In embodiments, wherein the bioreactor (G15) of FIG. 14G producedsynthetic cannabinoids from genetically modified photosyntheticmicroalgae and/or cyanobacterium, at least a portion of the geneticallymodified photosynthetic microalgae and/or cyanobacterium is filtered via(H11, H25, or H44 of FIG. 14H) and is then introduced into thecannabinoid extraction systems, either together with the cannabis orseparately or independently from the cannabis, described in Volume II,as depicted in FIGS. 17A′, 17A″, 17B′, 17C′, 17D″, 17H′. Alternately,the genetically modified photosynthetic microalgae and/or cyanobacteriummay be filtered and provided to a expeller press, or exposed to highpressure to extract cannabinoids therefrom.

In embodiments, the genetically modified microorganisms arephotosynthetic or autotrophic. In embodiments, the genetically modifiedmicroorganisms are autotrophic and produce their own food using light,water, carbon dioxide, or other chemicals. In embodiments, the culturemedium or liquid nutrient medium includes treated water and configuredto provide nourishment or environment necessary for growing thegenetically modified microorganisms. In embodiments, the culture mediumor liquid nutrient medium includes treated water and one or moreselected from the group consisting of carbon, carbon dioxide, oxygen,nitrogen, calcium, sulfur, sodium, potassium, iron, magnesium,phosphorous, calcium, zinc, fat, macronutrients, micronutrients,carbohydrates, sugars, an acid, a virus, and combinations thereof.

In embodiments, the present discloses relates to a method to produce abiosynthetic cannabinoid distillate, the method includes:

-   (a) in a photo-bioreactor, growing microalgae which have been    genetically modified to produce a biosynthetic cannabinoid, in a    liquid nutrient medium;-   (b) separating the grown, genetically modified microalgae from the    liquid nutrient medium;-   (c) extracting the biosynthetic cannabinoid from the grown,    genetically modified microalgae to produce an extracted biosynthetic    cannabinoid; and-   (d) distilling the extracted biosynthetic cannabinoid to produce the    biosynthetic cannabinoid distillate.

In embodiments, the biosynthetic cannabinoid distillate can be used toproduce a beverage, a nanoemulsion, a spray-dried water-soluble powderby spray drying the nanoemulsion. In embodiments, the biosyntheticcannabinoid and/or the biosynthetic cannabinoid distillate can mixedwith cannabis plant derived terpenes and/or non-biosynthetic plantderived cannabinoids. In embodiments, the biosynthetic cannabinoidand/or the biosynthetic cannabinoid distillate can mixed withnon-biosynthetic plant derived cannabinoids to produce new productshaving high quality and repeatability and uniformity.

In embodiments, the biosynthetic cannabinoid and/or the biosyntheticcannabinoid distillate can be used to produce a foodstuff from thebiosynthetic cannabinoid distillate, the foodstuff includes one or moreselected from the group consisting of ada, bagels, baked goods,beverages, biscuits, bitterballen, bonda, breads, cakes, candies,cereals, chips, chocolate bars, carbonated soft drinks, carbonateddrinks, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crêpes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, poffertjes, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,soft drinks, sport drinks, sparkling drinks, specialty milk, tele-bhaja,tempura, toffee, tortillas, totopo, turkish delights, or waffles. Inembodiments, the biosynthetic cannabinoid and/or the biosyntheticcannabinoid distillate can be used to produce a cosmetic product or atopical from the biosynthetic cannabinoid distillate.

In embodiments, the liquid nutrient medium includes treated water, thetreated water is treated with an adsorbent, ion exchange resin, and/or amembrane. In embodiments, the gas may be introduced to the liquidnutrient medium, the gas includes carbon dioxide. In embodiments, thephoto-bioreactor includes a superficial gas velocity ranging frombetween 0.1 to 15 inches per second, or 1 to 15, or 5 to 15, or 1 to 5inches per second. In embodiments, the liquid nutrient medium includesone or more selected from the group consisting of a carbohydrate, amicronutrient, a macronutrient, an acid, and combinations thereof.

In embodiments, the genetically modified microalgae are grown within aphoto-bioreactor at a residence time ranging from 1 to 5 days or 2 to 4days. In embodiments, the photo-bioreactor operates at a photosyntheticphoton flux density ranging from ranging from 50 to 1,000 micromole persecond and square meter. In embodiments, the photo-bioreactor isprovided with a photon flux density source including one or moreselected from the group consisting of compact fluorescent lights,incandescent lights, fluorescent lights, halogen lights, metal halidelamps, high-intensity discharge gas discharge lamps, low pressure sodiumlamps, sodium lamps, quartz halogen lamps, and combinations thereof. Inembodiments, the photo-bioreactor is provided with a photon flux densitysource light emitting diodes, wherein the light emitting diodes operateat a wave length ranging from 390 to 700 nanometers. In embodiments, thephoto-bioreactor is transparent and/or translucent. In embodiments, thephoto-bioreactor has a volume ranging from 50 to 2000 liters. Inembodiments, the extracted biosynthetic cannabinoid can be distilledwith via spinning band distillation, which is known to a person ofordinary skill in the art and available from a variety of commercialvendors including from: EquiLab Canada Inc., see B/R 9400 and 9600 HighEfficiency Distillation Systems, (http://www.equilabcanada.com); or fromhttps://www.alibaba.com, Model Number: HSPD-2000, 2L Turnkey SpinningBand Distillation Short Path Unit; or from BR Instrument, 9119Centreville Road Easton, Md. 21601 USA (https://brinstrument.com). Inembodiments, the spinning band distillation system is equipped todistill a variety of throughputs.

In embodiments, the spinning band distillation system is an automaticcontrolled distillation column having: a volume ranging from 1 to 2liters, 2 to 5 liters, 5 to 10 liters, 10 liters to 100 liters, 100liters to 1000 liters, 1000 liters to 1500 liters, 1500 liters to 5000liters; a column diameter ranging from 0.5 to 1 inch, 1 inch to 1.5inches, 1.5 inches to 2.5 inches, 2.5 inches to 3.5 inches, 3.5 inchesto 5 inches, 5 inches to 10 inches; a column length ranging from 5inches to 10 inches, 10 inches to 20 inches, 20 inches to 30 inches, 30inches to 40 inches, 40 inches to 50 inches, 50 inches to 60 inches, 60inches to 80 inches, 80 inches to 100 inches; maximum theoreticalplates, with a Teflon spinning band 10 to 15 maximum theoretical plates,15 to 30 maximum theoretical plates, 30 to 45 maximum theoreticalplates, 45 to 60 maximum theoretical plates; maximum theoretical plates,with a metal band 10 to 15 maximum theoretical plates, 15 to 30 maximumtheoretical plates, 30 to 45 maximum theoretical plates, 45 to 60maximum theoretical plates. In embodiments, the spinning banddistillation system operates in batch mode or continuously. Inembodiments, the spinning band distillation system includes a pluralityof spinning band distillation systems configured to operate in cyclicbatch mode.

In embodiments, the spinning band distillation system is steam heated,wherein the steam is generated from a boiler, wherein the boiler can beelectrically heated of natural gas heated. In embodiments, the spinningband distillation system is electrically heated and operates at avoltage of 110 volts, 120 volts, 220 volts. In embodiments, the spinningband distillation system operates under vacuum conditions.

In embodiments, the present discloses relates to a method to producebiosynthetic cannabinoid, the method includes:

-   (a) in a photo-bioreactor, growing microalgae and/or cyanobacterium    which have been genetically modified to produce a biosynthetic    cannabinoid, in a liquid nutrient medium and in the presence of    carbon dioxide, the liquid nutrient medium including water treated    with an adsorbent, ion exchange resin, and/or a membrane;-   (b) separating the grown, genetically modified microalgae and/or the    genetically modified cyanobacterium from the liquid nutrient medium;    and-   (c) extracting the biosynthetic cannabinoid from the grown,    genetically modified microalgae and/or the genetically modified    cyanobacterium to produce an extracted biosynthetic cannabinoid.

The present disclosure relates to methods to produce synthetic extractedand distilled cannabinoids and methods to prepare foods, drugs,chemicals, pharmaceuticals. One of ordinary skill in the art would knowhow to produce genetically modified microorganisms, as in geneticallymodified microalgae by viewing existing patents related to production ofgenetically modified microalgae as viewed in: WO2019210404 assigned toAlgae-C Inc. and titled Engineered Microorganism For The Production OfCannabinoid Biosynthetic Pathway Products.

FIG. 14I:

FIG. 14I shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to provide an insect-depleted liquid mixture(I19) and insects (I46).

FIG. 14I shows the liquid separation module (LSM) that is configured toremove liquid from the exoskeleton-depleted insect liquid mixture (H39)or the pressurized exoskeleton-depleted insect liquid mixture (H41).FIG. 14I shows the liquid separation module (LSM) configured to removeliquid from the exoskeleton-depleted insect liquid mixture (H39) that isprovided by the exoskeleton separation module (14H). FIG. 14I shows theliquid separation module (LSM) configured to remove liquid from thepressurized exoskeleton-depleted insect liquid mixture (H41) that isprovided by the exoskeleton separation module (14H). FIG. 14I shows onenon-limiting embodiment of a liquid separation module (LSM) thatincludes a filter (I11). FIG. 14J shows one non-limiting embodiment of aliquid separation module (LSM) that includes an evaporator (J11).

FIG. 14I shows an exoskeleton-depleted insect liquid mixture (H39) or apressurized exoskeleton-depleted insect liquid mixture (H41) transferredto the liquid separation module (LSM) from the exoskeleton separationmodule (14H) shown in FIG. 14H. The exoskeleton-depleted insect liquidmixture (H39) or a pressurized exoskeleton-depleted insect liquidmixture (H41) is transferred from the exoskeleton-depleted insect liquidmixture tank (H26) of FIG. 14H via the exoskeleton-depleted insectliquid mixture conduit (H38).

FIG. 14I displays the liquid separation module (LSM) including a liquidseparator (I10). In embodiments, the liquid separator (I10) is a filter(I11) or a membrane (I11A) having at least one side wall (I65). Inembodiments, the filter (I11) is cylindrical. In embodiments, the filter(I11) is a candle filter (I12) that has at least one filter element(I13) contained within its interior (I64). In embodiments, the filter(I11) has a top (I14) and a bottom (I15). FIG. 14I shows a separatorinput (I16) positioned on the side wall (I65) of the liquid separator(I10). The separator input (I16) is configured to introduce anexoskeleton-depleted insect liquid mixture (H39) or a pressurizedexoskeleton-depleted insect liquid mixture (H41) to the interior (I64)of the filter (I11). In embodiments, the exoskeleton-depleted insectliquid mixture (H39) or pressurized exoskeleton-depleted insect liquidmixture (H41) may be considered a liquid-laden insect mixture (I17).

A supply valve (I61) equipped with a controller (I62) and configured toinput and output a signal (I63) to the computer (COMP) is positioned onthe exoskeleton-depleted insect liquid mixture conduit (H38) in betweenthe exoskeleton-depleted insect liquid mixture tank (H26) of FIG. 14Hand the separator input (I16) positioned on the side wall (I65) of theliquid separator (I10) of FIG. 14I.

The filter (I11) has a first output (I18) positioned on the top (I14).The first output (I18) is configured to discharge an insect-depletedliquid mixture (I19) via an insect-depleted liquid mixture conduit(I20). A discharge valve (I21) equipped with a controller (I22) andconfigured to input and output a signal (I23) to the computer (COMP) ispositioned on the insect-depleted liquid mixture conduit (I20). Thefilter (I11) is configured to remove insects (I46) from either theexoskeleton-depleted insect liquid mixture (H39) or pressurizedexoskeleton-depleted insect liquid mixture (H41) to form aninsect-depleted liquid mixture (I19). The insect-depleted liquid mixture(I19) has a reduced amount of insects (I46) relative to theexoskeleton-depleted insect liquid mixture (H39) or pressurizedexoskeleton-depleted insect liquid mixture (H41).

The filter (I11) has a second output (I45) positioned on the bottom(I15). Insects (I46) may be separated from the exoskeleton-depletedinsect liquid mixture (H39) or pressurized exoskeleton-depleted insectliquid mixture (H41). A separated insect transfer conduit (I47) isconnected to the second output (I45) positioned on the bottom (I15) ofthe filter (I11). An insect conveyor (I48) is equipped to receiveinsects (I46) from the separated insect transfer conduit (I47).

An insect drying gas (I49) may be applied to a portion of the insects(I46) to remove any residual liquid therefrom and form liquid-depletedinsects (I50). In embodiments, the insect drying gas (I49) is heated toa temperature ranging from between 80 degrees F. to 90 degrees F.; 90degrees F. to 100 degrees F.; 100 degrees F. to 110 degrees F.; 110degrees F. to 120 degrees F.; 120 degrees F. to 140 degrees F.; 140degrees F. to 160 degrees F.; 160 degrees F. to 180 degrees F.; 180degrees F. to 200 degrees F.; 200 degrees F. to 250 degrees F.; 250degrees F. to 300 degrees F.; 300 degrees F. to 400 degrees F. Inembodiments, the liquid-depleted insects (ISO) may be routed to theinsect tank (G66) on FIG. 14G.

An insect discharge valve (I51) equipped with a controller (I52) andconfigured to input and output a signal (I53) to the computer (COMP) isinstalled on the separated insect transfer conduit (I47). A backflushfluid (I54) may be provided to the filter (I11) to regenerate the filterelement (I13). FIG. 14I shows the backflush fluid (I54) entering theinsect-depleted liquid mixture conduit (I20) and then entering theinterior (I64) of the filter (I11) via the first output (I18). Inembodiments, the backflush fluid (I54) is a liquid. In embodiments, thebackflush fluid (I54) is a gas.

A backflush fluid transfer conduit (I55) is connected to theinsect-depleted liquid mixture conduit (I20) via a connection (I70) inbetween the discharge valve (I21) and the first output (I18). Abackflush fluid supply valve (IH56) equipped with a controller (I57) andconfigured to input and output a signal (I58) to the computer (COMP) ispositioned on the backflush fluid transfer conduit (I55). Inembodiments, a backflush fluid pressure regulating valve (I59) with abackflush pressure sensor (I60) is positioned upstream of the backflushfluid supply valve (I56). In embodiments, the backflush fluid pressureregulating valve (I59) may be adjusted to a pressure that is less thanthe rupture pressure of that of the filter element (I13). It ispreferred to counter currently backflush the filter element (I13) bysetting the pressure of the backflush fluid pressure regulating valve(I59) to a pressure of 0.25 PSI to 0.5 PSI; 0.5 PSI to 1.5 PSI; 1.5 PSIto 3 PSI; 3 PSI to 6 PSI; 6 PSI to 9 PSI; 9 PSI to 15 PSI.

FIG. 14J:

FIG. 14J shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from the exoskeleton-depletedinsect liquid mixture (H39) to produce a vaporized liquid (J22) and astream of liquid-depleted insects (J10).

FIG. 14J shows the liquid separation module (LSM) that is configured toremove liquid from the exoskeleton-depleted insect liquid mixture (H39)or the pressurized exoskeleton-depleted insect liquid mixture (H41) toform a stream of liquid-depleted insects (J10). FIG. 14J shows theliquid separation module (LSM) configured to remove liquid from theexoskeleton-depleted insect liquid mixture (H39) that is provided by theexoskeleton separation module (14H). FIG. 14J shows the liquidseparation module (LSM) configured to remove liquid from the pressurizedexoskeleton-depleted insect liquid mixture (H41) that is provided by theexoskeleton separation module (14H).

FIG. 14J shows one non-limiting embodiment of a liquid separation module(LSM) that includes an evaporator (J11). FIG. 14J shows anexoskeleton-depleted insect liquid mixture (H39) or a pressurizedexoskeleton-depleted insect liquid mixture (H41) transferred to theliquid separation module (LSM) from the exoskeleton separation module(14H) shown in FIG. 14H. The exoskeleton-depleted insect liquid mixture(H39) or a pressurized exoskeleton-depleted insect liquid mixture (H41)is transferred from the exoskeleton-depleted insect liquid mixture tank(H26) of FIG. 14H via the exoskeleton-depleted insect liquid mixtureconduit (H38). FIG. 14J displays the liquid separation module (LSM)including a liquid separator (J10). In embodiments, the liquid separator(I10) is an evaporator (J11) which separates liquid by vaporizing theliquid.

In embodiments, the evaporator (J11) is a wiped-film evaporator (J11A).In embodiments, the evaporator (J11) is comprised of one or more fromthe group consisting of a rotary evaporator, falling film tubularevaporator, falling film evaporator, rising/falling film tubularevaporator, rising film tubular evaporator, rising film evaporator,forced circulation evaporator, internal pump forced circulationevaporator, plate evaporator, evaporative cooler, multiple-effectevaporator, thermal vapor recompression evaporator, mechanical vaporrecompression evaporator, flash tank, a crystallizer, a draft tube andbaffle crystallizer, cooling crystallization, evaporativecrystallization, fractional crystallization, and a distillation column,wherein the distillation column includes trays, packing, a wiper, or aspinning-band. The evaporator (J11) shown in FIG. 14J is that of awiped-film evaporator (J11A). The evaporator (J11) has a vapor inlet(J12), a separator input (J16), a heating jacket (J17), a first output(J18), and a second output (J19).

In embodiments, the evaporator (J11) includes a multiple effectevaporator. In embodiments, the multiple effect evaporator comprisesmore than one evaporator which may include any of the type ofevaporators listed herein. In embodiments, the multiple effectevaporator comprises two effect evaporators, three effect evaporators,four effect evaporators, five effect evaporators, six effectevaporators, seven effect evaporators, eight effect evaporators, or morethan eight effect evaporators. In embodiments, the multiple effectevaporator is segregated into multiple evaporator effects to removesolvent from the volatiles.

In embodiments, the evaporator (J11) is electrically heated. Inembodiments, the vapor inlet (J12) is provided with a vapor (J12A) suchas steam. In embodiments, the vapor (J12A) is a seventh steam supply(LDJ) that is provided from FIG. 14L. The vapor inlet is connected to avapor supply conduit (J13). A vapor supply valve (J14) is positioned onthe vapor supply conduit (J13). The vapor supply valve (J14) is equippedwith a controller (J15A) that is configured to input and output a signal(J15B) to the computer (COMP). In embodiments, the pressure drop acrossthe vapor supply valve (J14) ranges from between 5 PSI to 10 PSI, 15 PSIto 25 PSI, 25 PSI to 35 PSI, 35 PSI to 45 PSI, 45 PSI to 55 PSI, 55 PSIto 65 PSI, 65 PSI to 75 PSI, 75 PSI to 85 PSI. In embodiments, the vaporsupply valve (J14) percent open during normal operation ranges from 10%open to 25% open, 25% open to 35% open, 35% open to 45% open, 45% opento 55% open, 55% open to 65% open, 65% open to 75% open, 75% open to 80%open.

A separated vapor transfer conduit (J20) is connected to the firstoutput (J18) and is configured to transfer vaporized liquid (J22) fromthe evaporator (J11) to a condenser (J26). The condenser (J26) has avaporized liquid input (J25) that is configured to transfer thevaporized liquid (J22) from the separated vapor transfer conduit (J20)to the condenser (J26). The condenser (J26) is configured to acceptvaporized liquid (J22) from the evaporator (J11) and condense the liquidinto condensate (J27). Condensate (J27) is discharged from the condenser(J26) via a condenser condensate output (J30).

The condenser is connected to a vacuum system (J32) via a gas/vaportransfer conduit (J33). Gas/vapor (J35) is evacuated from the condenser(J27) via a gas/vapor discharge (J37). The gas/vapor (J35) transferredfrom the condenser to the vacuum system (J32) may be comprised of one ormore from the group consisting of carbon dioxide, nitrogen, air, steam,water vapor, and non-condensables. The vacuum system (J32) may be anyconceivable system configured to draw a vacuum on the condenser (J26).In embodiments, the vacuum system (J32) is that of a liquid-ring vacuumpump. A portion of the gas/vapor (J35) may be in turn condensed withinthe vacuum system (J26). A portion of the gas/vapor (J35) may bedischarged from the vacuum system (J26) via a gas/vapor transfer line(J39).

In embodiments, the vacuum system (J32) pulls a vacuum on the evaporator(J11) at a pressure ranging from 0.25 pounds per square inch absolute(PSIA) to 0.5 PSIA, 0.5 PSIA to 1 PSIA, 1 PSIA to 1.5 PSIA, 1.5 PSIA to3 PSIA, 3 PSIA to 4.5 PSIA, 4.5 PSIA to 6 PSIA, 6 PSIA to 7.5 PSIA, 7.5PSIA to 9 PSIA, 9 PSIA to 10.5 PSIA, 10.5 PSIA to 12 PSIA, 12 PSIA to13.5 PSIA, 12 PSIA to 12.25 PSIA, 12.25 PSIA to 12.5 PSIA, 12.5 PSIA to12.75 PSIA, 12.75 PSIA to 13 PSIA, 13 PSIA to 13.25 PSIA, 13.25 PSIA to13.5 PSIA, 13.5 PSIA to 13.75 PSIA, 13.75 PSIA to 14 PSIA, 14 PSIA to14.25 PSIA, 14.25 PSIA to 14.5 PSIA, or 14.5 PSIA to 14.75 PSIA. Thecondenser (J26) is provided with a cooling water input (J36) and acooling water output (J40). The cooling water input (J36) is configuredto accept a cooling water supply (J38) and the cooling water output(J40) is configured to discharge a cooling water return (J42). Thecooling water supply (J38) is configured to reduce the temperature ofthe vaporized liquid (J22) within the condenser (J26) to convert thevapor into a liquid condensate (J27).

The evaporator (J11) has an evaporator condensate output (J24) forevacuating condensate (J41) from the heating jacket (J17). Thecondensate (J41) discharged via the evaporator condensate output (J24)was provided to the evaporator heating jacket (J17) as the vapor (J12A)or steam. In embodiments, the evaporator condensate output (J24)discharges a seventh condensate (LAW) that is provided to the condensatetank (LAP) shown on FIG. 14L. The heating jacket (J17) accepts a sourceof vapor (J12A), and evaporates liquid from the exoskeleton-depletedinsect liquid mixture (H39) or the pressurized exoskeleton-depletedinsect liquid mixture (H41) to form vaporized liquid (J22) that isdischarged from the evaporator (J11) and sent to the condenser (J26).

In embodiments, the evaporator (J11) takes the form of a wiped-filmevaporator (J11A). In embodiments, the wiped-film evaporator (J11A) hasa motor (J42) and a wiper (J44). In embodiments, the motor (J42) andwiper (J44) act together to wipe at least one heat transfer surfacewithin the evaporator (J11).

The separator input (J16) is configured to introduce anexoskeleton-depleted insect liquid mixture (H39) or a pressurizedexoskeleton-depleted insect liquid mixture (H41) to the evaporator(J11). In embodiments, the exoskeleton-depleted insect liquid mixture(H39) or pressurized exoskeleton-depleted insect liquid mixture (H41)may be considered a liquid-laden insect mixture (117). The evaporatorvaporizes liquid from within the exoskeleton-depleted insect liquidmixture (H39) or pressurized exoskeleton-depleted insect liquid mixture(H41) to produce a vaporized liquid (J22) and a stream ofliquid-depleted insects (J10).

In embodiments, the liquid-depleted insects (J10) may be transferredfrom the evaporator (J11) and into a subsequent liquid removal system(J50), such as a belt press (J51) or a filter press (J61). The filterpress (J51) applies pressure to the liquid-depleted insects (J10) toseparate additional liquid (J52) therefrom and produce a subsequentliquid-depleted insects (J53) that have a reduced amount of liquid (J52)relative to the liquid-depleted insects (J10) that are discharged fromthe evaporator (J11). The subsequent liquid-depleted insects (J53) aretransferred from the filter press (J51) to a storage container (J54).

FIG. 14K:

FIG. 14K shows one non-limiting embodiment of a liquid separation module(LSM) that is configured to remove liquid from an insect liquid mixture(H39) by use of a spray dryer (KAP).

A plurality of separators separate at least a small insect particulateportion (KCW) and a large insect particulate portion (KCY) from aninsect and gas mixture (KBV) that is discharged in the drying chamber(KBG) of a spray dryer (KAP) evaporator (KAO). The spray dryer (KAP) istype of evaporator (KAO) that evaporates liquid from an insect liquidmixture (KAS). A first separator (KCA), second separator (KCI), and athird separator (KCR) are configured to accept an insect and gas mixture(KBV) from the drying chamber (KBG) of a spray dryer (KAP). Inembodiments, the first separator (KCA) is a cyclone or a filter. Inembodiments, the second separator (KCI) is a cyclone or a filter. Inembodiments, the third separator (KCR) is a sifter or a filter. Thethird separator (KCR) accepts first separated insects (KCG) from thefirst separator (KCA) and second separated insects (KCP) from the secondseparator (KCI) and separates at least a small insect particulateportion (KCW) and a large insect particulate portion (KCY) therefrom. Inembodiments, the small insect particulate portion (KCW) and a largeinsect particulate portion (KCY) are oligosaccharides or arehydrolyzed-biopolymers, as discussed above.

The exoskeleton-depleted insect liquid mixture conduit (H38) transfersan exoskeleton-depleted insect liquid mixture (H39) or an insect liquidmixture (KAS) to a liquid input (KAR) of the spray dryer (KAP). Thespray dryer (KAP) has a top (K-T) and a bottom (K-B). The spray dryer(KAP) has a vertical axis (KYY) and a horizontal axis (KXY). As shown inFIG. 14K, the liquid input (KAR) is located positioned towards the top(K-T) of the spray dryer (KAP). In embodiments, the liquid input (KAR)to the spray dryer (KAP) is positioned closer to the bottom (K-B) of thespray dryer (KAP). The pump (H40) on FIG. 14H transfers anexoskeleton-depleted insect liquid mixture (H39) or an insect liquidmixture (KAS) through the exoskeleton-depleted insect liquid mixtureconduit (H38) and into the liquid input (KAR) of the spray dryer (KAP).

In embodiments, the range of height of the drying chamber (KBG) isselected from one or more from the group 6 feet tall to 8 feet tall, 8feet tall to 10 feet tall, 10 feet tall to 12 feet tall, 12 feet tall to14 feet tall, 14 feet tall to 16 feet tall, 16 feet tall to 18 feettall, 18 feet tall to 20 feet tall, 20 feet tall to 22 feet tall, 22feet tall to 24 feet tall, 24 feet tall to 26 feet tall, 26 feet tall to28 feet tall, 28 feet tall to 30 feet tall, 30 feet tall to 32 feettall, 32 feet tall to 34 feet tall, 34 feet tall to 36 feet tall, 36feet tall to 38 feet tall, 38 feet tall to 40 feet tall, and 40 feettall to 50 feet tall.

In embodiments, the exoskeleton-depleted insect liquid mixture conduit(H38) connects the pump (H40) (on FIG. 14H) to: the evaporator (J11) onFIG. 14J; the wiped film evaporator (J11) on FIG. 14J; the evaporator(KAO) on FIG. 14J; the spray dryer (KAP) evaporator (KAO) on FIG. 14J.In embodiments, the exoskeleton-depleted insect liquid mixture conduit(H38) has heat tracing on it. In embodiments the heat tracing is poweredby electricity.

In embodiments, the range of diameter of the drying chamber (KBG) isselected from one or more from the group 2 feet in diameter to 4 feet indiameter, 4 feet in diameter to 6 feet in diameter, 6 feet in diameterto 8 feet in diameter, 8 feet in diameter to 10 feet in diameter, 10feet in diameter to 12 feet in diameter, 12 feet in diameter to 14 feetin diameter, 14 feet in diameter to 16 feet in diameter, 16 feet indiameter to 18 feet in diameter, 18 feet in diameter to 20 feet indiameter, 20 feet in diameter to 22 feet in diameter, 22 feet indiameter to 24 feet in diameter, 24 feet in diameter to 26 feet indiameter, 26 feet in diameter to 28 feet in diameter, 28 feet indiameter to 30 feet in diameter, 30 feet in diameter to 32 feet indiameter, 32 feet in diameter to 34 feet in diameter, 34 feet indiameter to 36 feet in diameter, 36 feet in diameter to 38 feet indiameter, and 38 feet in diameter to 40 feet in diameter. Inembodiments, the drying chamber (KBG) is comprised of a material that isselected from one or more from the group consisting of carbon steel,graphite, Hastelloy alloy, nickel, stainless steel, tantalum, andtitanium.

An insect/liquid mixture flow sensor (KEQ) is positioned on the conduit(H38) prior to the spray dryer (KAP). The insect/liquid mixture flowsensor (KEQ) is configured to input or output a signal (KER) to thecomputer (COMP). The insect/liquid mixture flow sensor (KEQ) measuresthe flow of the insect liquid mixture (H39, KAS) that is introduced tothe liquid input (KAR) of the spray dryer (KAP). An insect/liquidmixture valve (KEC) is positioned on the conduit (H38) prior to thespray dryer (KAP). The insect/liquid mixture valve (KEC) has acontroller (KED) that is configured to input or output a signal (KEE) tothe computer (COMP). The insect/liquid mixture valve (KEC) and theinsect/liquid mixture flow sensor (KEQ) may be used together in a flowcontrol loop to set the flowrate of spray dryer (KAP) to a flow ratethat includes one or more from the group consisting of: 0.5 gallons perminute (GPM) to 1 GPM, 1 GPM to 1.5 GPM, 1.5 GPM to 2 GPM, 2 GPM to 2.5GPM, 2.5 GPM to 3 GPM, 3 GPM to 3.5 GPM, 3.5 GPM to 4 GPM, 4 GPM to 4.5GPM, 4.5 GPM to 5 GPM, 5 GPM to 5.5 GPM, 5.5 GPM to 6 GPM, 6 GPM to 6.5GPM, 6.5 GPM to 7 GPM, 7 GPM to 7.5 GPM, 7.5 GPM to 8 GPM, 8 GPM to 8.5GPM, 8.5 GPM to 9 GPM, 9 GPM to 9.5 GPM, 9.5 GPM to 10 GPM, and 10 GPMto 10.5 GPM.

In embodiments, the water content of the insect liquid mixture (KAS)that is transferred to the mixture input (KAR) of the spray dryer (KAP)ranges between 40 weight percent liquid and 85 weight percent liquid. Inembodiments, the water content of the insect liquid mixture (KAS) thatis transferred to the mixture input (KAR) of the spray dryer (KAP)ranges between 45 weight percent liquid and 80 weight percent liquid.However, other mixture rations might work such as insect to liquidratios selected from one or more from the group consisting of 1:9, 3:17,1:4, 1:3, 3:7, 7:13, 2:3, 9:11, 1:1, 1.22:1, 1.5:1, 1.86:1, and 2.33:1.In embodiments, the ratio of pounds of insects divided by pounds ofliquid may be selected from one or more from the group consisting of0.11, 0.18, 0.25, 0.33, 0.43, 0.54, 0.67, 0.82, 1.00, 1.22, 1.50, 1.86,and 2.33. In embodiments, insect liquid mixture (KAS) may have a ratioof pounds of liquid divided by pounds of insects that is selected fromone or more from the group consisting of 9.0, 5.6, 4.0, 3.0, 2.3, 1.8,1.5, 1.2, 1.0, 0.8, 0.6, 0.5, 0.4, and 0.3.

In embodiments, the exoskeleton-depleted insect liquid mixture (H39) orthe insect liquid mixture (KAS) is pressurized. An inlet pressure sensor(KBE) is positioned on the conduit (H38) prior to the spray dryer (KAP).The inlet pressure sensor (KBE) measures the pressure of the insectliquid mixture (H39, KAS) that is introduced to the liquid input (KAR)of the spray dryer (KAP). The inlet pressure sensor (KBE) transmits asignal (KBF) to the computer (COMP).

In embodiments, the range of pressure that the inlet pressure sensor(KBE) transmits to the computer (COMP) ranges from one or more from thegroup consisting of: 5 pounds per square inch (PSI) to 10 PSI; 10 PSI to15 PSI; 15 PSI to 20 PSI; 20 PSI to 25 PSI; 25 PSI to 30 PSI; 30 PSI to35 PSI; 35 PSI to 40 PSI; 40 PSI to 45 PSI; 45 PSI to 50 PSI; 50 PSI to55 PSI; 55 PSI to 60 PSI; 60 PSI to 65 PSI; 65 PSI to 70 PSI; 70 PSI to75 PSI; 75 PSI to 80 PSI; 80 PSI to 85 PSI; 85 PSI to 90 PSI; 90 PSI to95 PSI; 95 PSI to 100 PSI; 100 PSI to 125 PSI; 125 PSI to 145 PSI; 145PSI to 170 PSI; 170 PSI to 195 PSI; 195 PSI to 200 PSI; 200 PSI to 220PSI; 220 PSI to 250 PSI; 250 PSI to 275 PSI; 275 PSI to 300 PSI; 300 PSIto 350 PSI; 350 PSI to 402 PSI; 402 PSI to 463 PSI; 463 PSI to 532 PSI;532 PSI to 612 PSI; 612 PSI to 704 PSI; 704 PSI to 809 PSI; 809 PSI to930 PSI; 930 PSI to 1070 PSI; 1,070 PSI to 1,231 PSI; 1,231 PSI to 1,415PSI; 1,415 PSI to 1,627 PSI; 1,627 PSI to 1,872 PSI; 1,872 PSI to 2,152PSI; 2,152 PSI to 2,475 PSI; 2,475 PSI to 2,846 PSI; 2,846 PSI to 3,273PSI; 3,273 PSI to 3,764 PSI; 3,764 PSI to 4,329 PSI; 4,329 PSI to 4,978PSI; 4,978 PSI to 5,725 PSI; 5,725 PSI to 6,584 PSI; 6,584 PSI to 7,571PSI; 7,571 PSI to 8,707 PSI; 8,707 PSI to 10,013 PSI; 10,013 PSI to11,515 PSI; and 11,515 PSI to 15,000 PSI.

In embodiments, the residence time of the insect liquid mixture (KAS)and gas supply (KAG) within the spray dryer (KAP) or drying chamber(KBG) ranges from one or more from the group selected from: 0.1 secondsto 1 seconds, 1 seconds to 2 seconds, 2 seconds to 3 seconds, 3 secondsto 4 seconds, 4 seconds to 5 seconds, 5 seconds to 6 seconds, 6 secondsto 7 seconds, 7 seconds to 8 seconds, 8 seconds to 9 seconds, 9 secondsto 10 seconds, 10 seconds to 12 seconds, 12 seconds to 15 seconds, 15seconds to 20 seconds, 20 seconds to 25 seconds, 25 seconds to 30seconds, 30 seconds to 35 seconds, 35 seconds to 40 seconds, 40 secondsto 45 seconds, 45 seconds to 50 seconds, 50 seconds to 55 seconds, 55seconds to 60 seconds, 60 seconds to 65 seconds, 65 seconds to 70seconds, 70 seconds to 80 seconds, 80 seconds to 90 seconds, 90 secondsto 100 seconds, 100 seconds to 110 seconds, and 110 seconds to 120seconds.

A gas supply (KAG) is made available to the spray dryer (KAP) via a gasinput (KAQ). In embodiments, the gas supply (KAG) may include a gas. Inembodiments, the gas supply (KAG) may include a carbon dioxide. Inembodiments, the gas supply (KAG) may include air. In embodiments, thegas supply (KAG) may include an oxygen-containing gas which includesair, oxygen-enriched-air i.e. greater than 21 mole % O2, andsubstantially pure oxygen, i.e. greater than about 95 mole % oxygen (theremainder usually comprising N2 and rare gases). In embodiments, the gassupply (KAG) may include flue gas which includes a vapor or gaseousmixture containing varying amounts of nitrogen (N2), carbon dioxide(CO2), water (H2O), and oxygen (O2). Flue gas is generated from thethermochemical process of combustion. In embodiments, the gas supply(KAG) may include a combustion stream.

A filter (KAH) is made available to remove particulates from the gassupply (KAG) prior to being introduced to the gas input (KAQ) of thespray dryer (KAP). A filter (KAH) may include a sorbent (KAH′) and beconfigured to adsorb and/or absorb at least one component that iscontained within the gas supply (KAG) prior to being introduced to thegas input (KAQ) of the spray dryer (KAP). In embodiments, the filter(KAH) may be a dehumidifier. In embodiments, the filter (KAH) may removewater from the gas supply (KAG) using an adsorbent. In embodiments, theadsorbent used in the filter (KAH) be selected from one or more from thegroup consisting of 3 Angstrom molecular sieve, 3 Angstrom zeolite, 4Angstrom molecular sieve, 4 Angstrom zeolite, activated alumina,activated carbon, adsorbent, alumina, carbon, catalyst, clay, desiccant,molecular sieve, polymer, resin, and silica gel. In embodiments, thefilter (KAH) may include any conceivable means to remove moisture fromthe gas supply (KAG), such as an air conditioner, cooling tower, anadsorber, a plurality of adsorbers. In embodiments, the filter (KAH) mayinclude a cooling tower followed by an adsorber. In embodiments, thefilter (KAH) may include a cooling tower followed by a plurality ofadsorbers. In embodiments, an adsorber is a packed bed of adsorbent. Inembodiments, an adsorber is a moving bed of adsorbent. In embodiments,an adsorber contains an adsorbent.

A fan (KAI) is made available and is configured to introduce the gassupply (KAG) to the spray dryer (KAP). The fan (KAI) is equipped with amotor (KAJ) that has a controller (KAK) which is configured to input oroutput a signal (KAL) to the computer (COMP). In embodiments, the fan(KAI) operates within a range that is selected from one or more from thegroup consisting of: 350 standard cubic feet per minute (SCFM) to 3,500SCFM; 700 SCFM to 7,000 SCFM; 1,050 SCFM to 10,500 SCFM; 1,400 SCFM to14,000 SCFM; 1,750 SCFM to 17,500 SCFM; 2,100 SCFM to 21,000 SCFM; 2,450SCFM to 24,500 SCFM; 2,800 SCFM to 28,000 SCFM; 3,150 SCFM to 31,500SCFM; 3,500 SCFM to 35,000 SCFM; 3,850 SCFM to 38,500 SCFM; 4,200 SCFMto 42,000 SCFM; 4,550 SCFM to 45,500 SCFM; 4,900 SCFM to 49,000 SCFM;5,250 SCFM to 52,500 SCFM; 5,600 SCFM to 56,000 SCFM; 5,950 SCFM to59,500 SCFM; 6,300 SCFM to 63,000 SCFM; 6,650 SCFM to 66,500 SCFM; 7,000SCFM to 70,000 SCFM; and 7,350 SCFM to 73,500 SCFM.

In embodiments, at an insect liquid mixture flow rate of 0.5 to 1 GPM,the fan (KAI) operates in a range between 350 standard cubic feet perminute (SCFM) to 3,500 SCFM. In embodiments, at an insect liquid mixtureflow rate of 0.5 to 1 GPM, the fan (KAI) operates in a range between 700SCFM to 7,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 1 to 1.5 GPM, the fan (KAI) operates in a range between 1,050SCFM to 10,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 1.5 to 5 GPM, the fan (KAI) operates in a range between 1,400SCFM to 14,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 2 to 2.5 GPM, the fan (KAI) operates in a range between 1,750SCFM to 17,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 2.5 to 3 GPM, the fan (KAI) operates in a range between 2,100SCFM to 21,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 3 to 3.5 GPM, the fan (KAI) operates in a range between 2,450SCFM to 24,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 3.5 to 4 GPM, the fan (KAI) operates in a range between 2,800SCFM to 28,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 4 to 4.5 GPM, the fan (KAI) operates in a range between 3,150SCFM to 31,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 4.5 to 5 GPM, the fan (KAI) operates in a range between 3,500SCFM to 35,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 5 to 5.5 GPM, the fan (KAI) operates in a range between 3,850SCFM to 38,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 5.5 to 6 GPM, the fan (KAI) operates in a range between 4,200SCFM to 42,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 6 to 6.5 GPM, the fan (KAI) operates in a range between 4,550SCFM to 45,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 6.5 to 7 GPM, the fan (KAI) operates in a range between 4,900SCFM to 49,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 7 to 7.5 GPM, the fan (KAI) operates in a range between 5,250SCFM to 52,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 7.5 to 8 GPM, the fan (KAI) operates in a range between 5,600SCFM to 56,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 8 to 8.5 GPM, the fan (KAI) operates in a range between 5,950SCFM to 59,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 8.5 to 9 GPM, the fan (KAI) operates in a range between 6,300SCFM to 63,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 9 to 9.5 GPM, the fan (KAI) operates in a range between 6,650SCFM to 66,500 SCFM. In embodiments, at an insect liquid mixture flowrate of 9.5 to 10 GPM, the fan (KAI) operates in a range between 7,000SCFM to 70,000 SCFM. In embodiments, at an insect liquid mixture flowrate of 10 to 10.5 GPM, the fan (KAI) operates in a range between 7,350SCFM to 73,500 SCFM.

An air heater (KAF) is made available to heat the gas supply (KAG) priorto being introduced to the gas input (KAQ) of the spray dryer (KAP).FIG. 14K shows the gas supply (KAG) first entering the filter (KAH),then the fan (KAI), and then the air heater (KAF). It is to be notedthat combinations of the filter (KAH), fan (KAI), and air heater (KAF)shown in FIG. 14K are non-limiting. For example, the fan (KAI) may bebefore the filter (KAH), the fan (KAI) may be after the air heater(KAF), the filter (KAH) may be after the fan (KAI), the filter (KAH) maybe after the air heater (KAF), the air heater (KAF) may be before thefan (KAI). The air heater (KAF) provides a heated gas supply (KAG) tothe spray dryer (KAP).

In embodiments, the ideal range that the temperature sensor (KAM) inputsinto the computer (COMP) while measuring the heated gas supply (KAG) ispreferably set to 250 degrees Fahrenheit to 600 degrees Fahrenheit, butmore preferably to 300 degrees Fahrenheit to 5000 degrees Fahrenheit,but more preferably to 350 degrees Fahrenheit to 450 degrees Fahrenheit.In embodiments, the heated gas supply (KAG) has a temperature selectedfrom the group consisting of: 250 degrees Fahrenheit to 275 degreesFahrenheit; 275 degrees Fahrenheit to 300 degrees Fahrenheit; 300degrees Fahrenheit to 325 degrees Fahrenheit; 325 degrees Fahrenheit to350 degrees Fahrenheit; 350 degrees Fahrenheit to 375 degreesFahrenheit; 375 degrees Fahrenheit to 400 degrees Fahrenheit; 400degrees Fahrenheit to 425 degrees Fahrenheit; 425 degrees Fahrenheit to450 degrees Fahrenheit; 450 degrees Fahrenheit to 475 degreesFahrenheit; 475 degrees Fahrenheit to 500 degrees Fahrenheit; 500degrees Fahrenheit to 525 degrees Fahrenheit; 525 degrees Fahrenheit to550 degrees Fahrenheit; 550 degrees Fahrenheit to 575 degreesFahrenheit; 575 degrees Fahrenheit to 600 degrees Fahrenheit; 600degrees Fahrenheit to 625 degrees Fahrenheit; 625 degrees Fahrenheit to650 degrees Fahrenheit; 650 degrees Fahrenheit to 675 degreesFahrenheit; 675 degrees Fahrenheit to 700 degrees Fahrenheit; 700degrees Fahrenheit to 725 degrees Fahrenheit; 725 degrees Fahrenheit to750 degrees Fahrenheit; 750 degrees Fahrenheit to 775 degreesFahrenheit; and 775 degrees Fahrenheit to 800 degrees Fahrenheit.

The temperature sensor (KAM) is configured to input a signal (KAN) tothe computer (COMP). The computer (COMP), temperature sensor (KAM), andthe motor (KAJ) of the fan (KAI) may be used together in a temperaturecontrol loop to maintain a constant pre-determined temperature of heatedgas to the spray dryer (KAP).

In embodiments, the heated gas supply (KAG) is created by indirectcontact with steam in the air heater (KAF). In embodiments, the airheater (KAF) may be electrically heated or heated by a combustion steamor flue gas. The heated gas supply (KAG) may also be a combustionstream. In embodiments, the air heater (KAF) accepts a source of steamfrom a steam drum (LBE) as shown on FIG. 14L. The steam drum (LBE)provides an eighth steam supply (LDM) to the air heater (KAF), asdiscussed below. The eighth steam supply (LDM) may be saturated orsuperheated steam. A steam flow control valve (KAA) is configured toregulate the flow of the steam that passes through the air heater (KAF).The steam flow control valve (KAA) is equipped with a controller (KAB)that sends a signal (KAC) to or from the computer (COMP).

A flow sensor (KAD) is configured to measure the flow of the steam thatpasses through the air heater (KAF). The flow sensor (KAD) sends asignal (KAE) to the computer (COMP). The computer (COMP), steam flowcontrol valve (KAA), and the flow sensor (KAD) may be used in a controlloop to control the flow of steam that is passed through the air heater(KAF). In embodiments, the computer (COMP), steam flow control valve(KAA), flow sensor (KAD), temperature sensor (KAM), and motor (KAJ) ofthe fan (KAI) may be used together in a temperature control loop tomaintain a constant pre-determined temperature of heated gas to thespray dryer (KAP). The steam flow control valve (KAA) may be positionedbefore or after the air heater (KAF). The air heater (KAF) discharges aneighth condensate (LJA) to the condensate tank (LAP) that is shown onFIG. 14L. A condensate temperature sensor (KK1) is configured to measurethe temperature of the eighth condensate (LJA) that leaves the airheater (KAF). The condensate temperature sensor (KK1) sends a signal(KK2) to the computer (COMP).

In embodiments, the liquid separation module (LSM) separates liquid fromthe insect and liquid mixture (H39, KAS) by converting the liquid into avapor. In embodiments, the liquid separation module (LSM) evaporatesliquid from within the insect and liquid mixture (H39, KAS) by use of anevaporator (KAO). A spray dryer (KAP) is a type of evaporator (KAO).

In embodiments, the spray dryer (KAP) evaporator (KAO) operates at atemperature greater than the boiling point of the liquid within theinsect and liquid mixture (H39, KAS) to vaporize the liquid portion ofthe insect and liquid mixture (H39, KAS) into a vapor. In embodiments,the spray dryer (KAP) is configured to mix a heated gas supply (KAG′)with an insect liquid mixture (H39, KAS) under precise computer operatedautomated control to generate an insect and gas mixture (KBV).

In embodiments, the spray dryer (KAP) has an interior (KAP′) whichaccepts both the heated gas supply (KAG′) and the insect liquid mixture(H39, KAS). In embodiments, the spray dryer (KAP) has an interior (KAP′)which accepts both the heated gas supply (KAG′) via the gas input (KAQ)and the insect liquid mixture (H39, KAS) via the liquid input (KAR). Inembodiments, the spray dryer (KAP) is equipped with a plurality of spraynozzles (KBC) that dispense the insect liquid mixture (H39, KAS) withinthe interior (KAP′) of the spray dryer (KAP).

In embodiments the spray dryer (KAP) has a drying chamber (KBG) whichevaporates liquid within the insect liquid mixture (H39, KAS). Inembodiments, interior (KBG′) of the drying chamber (KBG) is locatedwithin the interior (KAP′) of the spray dryer (KAP). In embodiments thespray dryer (KAP) has an air distributor (KAT) that is configured toaccept the heated gas supply (KAG′) from the gas input (KAQ) anddistribute it to the interior (KAP′) of the drying chamber (KBG). Inembodiments, the heated gas supply (KAG′) is introduced to the interior(KAP′) of the spray dryer (KAP) via the air distributor (KAT) usingcentrifugal momentum.

In embodiments, the insect liquid mixture (H39, KAS) is introduced tothe interior (KAP′) of the spray dryer (KAP) via a plurality of spraynozzles (KBC). In embodiments, the insect liquid mixture (H39, KAS) isintroduced to the interior (KBG′) of the drying chamber (KBG) via aplurality of spray nozzles (KBC). In embodiments, the insect liquidmixture (H39, KAS) is introduced to the interior (KAP′) of the spraydryer (KAP) via a rotary atomizer (KAU) which may have a spray nozzle(KBC) or a plurality of spray nozzles (KBC). In embodiments, the insectliquid mixture (H39, KAS) is introduced to the interior (KBG′) of thedrying chamber (KBG) via a rotary atomizer (KAU). In embodiments, therotary atomizer (KAU) dispenses insect liquid mixture (H39, KAS) orstart-up liquid (KEO) into the interior (KBG′) of the drying chamber(KBG) via an opening (KBD) or a plurality of openings (KBD) or a spraynozzle (KBC) or a plurality of spray nozzles (KBC).

In embodiments the pressure drop across the opening (KBD), plurality ofopenings (KBD), spray nozzle (KBC), or plurality of spray nozzles (KBC)includes one or more from the group consisting of: 5 pounds per squareinch (PSI) to 10 PSI; 10 PSI to 15 PSI; 15 PSI to 20 PSI; 20 PSI to 25PSI; 25 PSI to 30 PSI; 30 PSI to 35 PSI; 35 PSI to 40 PSI; 40 PSI to 45PSI; 45 PSI to 50 PSI; 50 PSI to 55 PSI; 55 PSI to 60 PSI; 60 PSI to 65PSI; 65 PSI to 70 PSI; 70 PSI to 75 PSI; 75 PSI to 80 PSI; 80 PSI to 85PSI; 85 PSI to 90 PSI; 90 PSI to 95 PSI; 95 PSI to 100 PSI; 100 PSI to125 PSI; 125 PSI to 145 PSI; 145 PSI to 170 PSI; 170 PSI to 195 PSI; 195PSI to 200 PSI; 200 PSI to 220 PSI; 220 PSI to 250 PSI; 250 PSI to 275PSI; 275 PSI to 300 PSI; 300 PSI to 350 PSI; 350 PSI to 402 PSI; 402 PSIto 463 PSI; 463 PSI to 532 PSI; 532 PSI to 612 PSI; 612 PSI to 704 PSI;704 PSI to 809 PSI; 809 PSI to 930 PSI; 930 PSI to 1070 PSI; 1,070 PSIto 1,231 PSI; 1,231 PSI to 1,415 PSI; 1,415 PSI to 1,627 PSI; 1,627 PSIto 1,872 PSI; 1,872 PSI to 2,152 PSI; 2,152 PSI to 2,475 PSI; 2,475 PSIto 2,846 PSI; 2,846 PSI to 3,273 PSI; 3,273 PSI to 3,764 PSI; 3,764 PSIto 4,329 PSI; 4,329 PSI to 4,978 PSI; 4,978 PSI to 5,725 PSI; 5,725 PSIto 6,584 PSI; 6,584 PSI to 7,571 PSI; 7,571 PSI to 8,707 PSI; 8,707 PSIto 10,013 PSI; 10,013 PSI to 11,515 PSI; and 11,515 PSI to 15,000 PSI.

The rotary atomizer (KAU) has a motor (KAV) and a controller (KAW) thatis configured to input or output a signal (KAX) to the computer (COMP).In embodiments, the motor (KAV) of the rotary atomizer (KAU) isconnected to a shaft (KBA). In embodiments, the shaft (KBA) is connectedto a disc (KBB). In embodiments, the disc (KBB) has an opening (KBD) ora plurality of openings (KBD) or spray nozzle (KBC) or a plurality ofspray nozzles (KBC) installed on it. In embodiments, the motor (KAV)rotates the shaft (KBA) which in turn rotates the disc (KBB) and thendistributes the insect liquid mixture (KAS) or start-up liquid (KEO) tothe interior (KAP′) of the spray dryer (KAP) or the interior (KBG′) ofthe drying chamber (KBG).

In embodiments, the spray nozzle (KBC) or plurality of spray nozzles(KBC) each have an opening (KBD). In embodiments, the spray nozzle (KBC)or plurality of spray nozzles (KBC) each have a spray aperture (KK4). Inembodiments, the spray nozzle (KBC) or plurality of spray nozzles (KBC)each have an orifice (KK5). In embodiments, the spray nozzle (KBC) orplurality of spray nozzles (KBC) each have an impingement surface (KK6).

In embodiments, at least a portion of the insect liquid mixture (H39,KAS) or start-up liquid (KEO) contact an impingement surface (KK6) priorto being dispensed to the interior (KAP′) of the spray dryer (KAP) orthe interior (KBG′) of the drying chamber (KBG) via a spray aperture(KK4). In embodiments, at least a portion of the insect liquid mixture(H39, KAS) or start-up liquid (KEO) pass through an orifice (KK5) priorto being dispensed to the interior (KAP′) of the spray dryer (KAP) orthe interior (KBG′) of the drying chamber (KBG) via a spray aperture(KK4). In embodiments, at least a portion of the insect liquid mixture(H39, KAS) or start-up liquid (KEO) pass through the spray nozzle (KBC)or plurality of spray nozzles (KBC) and contact an orifice (KK5) priorto being dispensed to the interior (KAP′) of the spray dryer (KAP) orthe interior (KBG′) of the drying chamber (KBG).

In embodiments, the plurality of spray nozzles (KBC) have a spraypattern is a hollow cone, full cone, or a flat spray. In embodiments,the spray pattern includes is that of the whirling type. In embodiments,the whirling type spray nozzle sprays the insect liquid mixture (H39,KAS) or start-up liquid (KEO) while rotating the liquid (H39, KAS, KEO)across a portion of the spray nozzle (KBC). A whirling type spray nozzle(KBC) is one that sprays the insect liquid mixture (H39, KAS) orstart-up liquid (KEO) while rotating the liquid (H39, KAS, KEO) across aportion of the spray nozzle (KBC) after a pressure drop has taken place.A whirling type spray nozzle (KBD) is one that sprays the insect liquidmixture (H39, KAS) or start-up liquid (KEO) while rotating the liquid(H39, KAS, KEO) across a portion of the spray nozzle after the liquid orslurry has passed through an orifice.

In embodiments, a whirling type spray nozzle (KBD) includes an orifice(KK5) and an impingement surface (KK6): the orifice (KK5) is configuredto accept insect liquid mixture (H39, KAS) or start-up liquid (KEO) anddrop the pressure from a first higher pressure to a second lowerpressure, the first pressure being greater than the second pressure; animpingement surface (KK6) that is configured to accept the liquid (H39,KAS, KEO) at the second pressure at change its direction to impartrotational or centrifugal momentum.

A whirling type spray nozzle (KBD) is one that sprays a liquid (H39,KAS, KEO) under cyclone conditions. In embodiments, the spray nozzle(KBD) is comprised of ceramic, metal, brass, 316 stainless steel, 316Lstainless steel, stainless steel, polytetrafluoroethylene (PTFE), orplastic, or a composite material. In embodiments, the spray nozzle (KBC)opening (KBD) ranges from 0.030 inches to 0.30 inches. In embodiments,the spray nozzle (KBC) opening (KBD) ranges from 0.03 inches to 0.16inches. In embodiments, the spray nozzle (KBC) orifice (KK5) ranges from0.030 inches to 0.30 inches. In embodiments, the spray nozzle (KBC)orifice (KK5) ranges from 0.03 inches to 0.16 inches.

In embodiments, the spray nozzle (KBC) has an orifice (KK5) and a sprayaperture (KK4). In embodiments, the spray angle of the spray nozzle(KBC) ranges from 15° to 120°. In embodiments, the spray angle of thespray nozzle (KBC) ranges from 30° to 100°. In embodiments, the sprayangle of the spray nozzle (KBC) ranges from 40° to 90°. In embodiments,the spray angle of the spray nozzle (KBC) ranges from 50° to 85°. Inembodiments, the spray angle of the spray nozzle (KBC) ranges from 70°to 75°. In embodiments, the spray angle of the spray nozzle (KBC) rangesfrom 45° to 89°. In embodiments, the spray angle of the spray nozzle(KBC) ranges from 90° to 134°. In embodiments, the spray angle of thespray nozzle (KBC) ranges from 135° to 179°. In embodiments, the sprayangle of the spray nozzle ranges (KBC) from 180° to 360°.

In embodiments, the spray nozzle (KBC) creates solid insect particulatesthat have a size selected from one or more from the group consisting of:10 microns to 2,000 microns, 20 microns to 1,900 microns, 40 microns to1,600 microns, 50 microns to 1,200 microns, 50 microns to 1,000 microns,35 microns to 225 microns, 50 microns to 500 microns, 100 microns to2,000 microns, and 75 microns to 1,000 microns.

In embodiments, the spray nozzle (KBC) creates solid insect particulatesthat have a size selected from one or more from the group consisting of:0.001 microns to 0.002 microns; 0.002 microns to 0.004 microns; 0.004microns to 0.008 microns; 0.008 microns to 0.016 microns; 0.016 micronsto 0.032 microns; 0.032 microns to 0.064 microns; 0.064 microns to 0.122microns; 0.128 microns to 0.251 microns; 0.256 microns to 0.512 microns;0.512 microns to 1.0 microns; 1.0 microns to 1.5 microns; 1.5 microns to2.3 microns; 2.3 microns to 3.5 microns; 3.5 microns to 5.2 microns; 5.2microns to 7.8 microns; 7.8 microns to 12 microns; 12 microns to 17microns; 17 microns to 26 microns; 26 microns to 39 microns; 39 micronsto 59 microns; 59 microns to 89 microns; 89 microns to 133 microns; 133microns to 199 microns; 199 microns to 299 microns; 299 microns to 448microns; 448 microns to 673 microns; 673 microns to 1009 microns; 1009microns to 1513 microns; 1513 microns to 2270 microns; 2270 microns to3405 microns; 3405 microns to 5108 microns; and 5108 microns to 7661microns.

In embodiments, each spray nozzle (KBC) is affixed to the disc (KAB)using one or more connectors selected from the group consisting ofnational pipe thread, British standard pipe thread, and welded. Inembodiments, the spray nozzle (KBC) is connected to the disc (KAB) using0.25 inch national pipe threads, 0.375 inch national pipe threads, 0.50inch national pipe threads, 0.625 inch national pipe threads, 0.75 inchnational pipe threads, 1 inch national pipe threads, 1.25 inch nationalpipe threads, 1.375 inch national pipe threads, 1.625 inch national pipethreads, 1.75 inch national pipe threads, 1.875 inch national pipethreads, or 2 inch national pipe threads. In embodiments, the spraynozzle (KBC) is connected to the disc (KAB) using a fitting thatincludes 0.25 inch pipe threads, 0.375 inch pipe threads, 0.50 inch pipethreads, 0.625 inch pipe threads, 0.75 inch pipe threads, 1 inch pipethreads, 1.25 inch pipe threads, 1.375 inch pipe threads, 1.625 inchpipe threads, 1.75 inch pipe threads, 1.875 inch pipe threads, or 2 inchpipe threads.

In embodiments, the flow through the disc (KAB) is selected from one ormore from the group consisting of 30 gallons per hour to 90 gallons perhour, 90 gallons per hour to 210 gallons per hour, 210 gallons per hourto 330 gallons per hour, 330 gallons per hour to 450 gallons per hour,and 450 gallons per hour to 630 gallons per hour.

In embodiments, the disc (KAB) is has a plurality of spray nozzles(KBC), the plurality of spray nozzles (KBC) is comprised of a quantityof spray nozzles that is selected from one or more from the groupconsisting of 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17,18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35,36, 37, 38, 39, 40, 41, and 42 spray nozzles.

In embodiments, the disc (KAB) is has a plurality of spray nozzles(KBC), the quantity of spray nozzles (KBC) that are installed on thedisc (KAB) is selected from one or more from the group consisting of: 1spray nozzles to 3 spray nozzles, 3 spray nozzles to 6 spray nozzles, 6spray nozzles to 9 spray nozzles, 9 spray nozzles to 12 spray nozzles,12 spray nozzles to 15 spray nozzles, 15 spray nozzles to 18 spraynozzles, 18 spray nozzles to 21 spray nozzles, 21 spray nozzles to 24spray nozzles, 24 spray nozzles to 27 spray nozzles, 27 spray nozzles to30 spray nozzles, 30 spray nozzles to 33 spray nozzles, 33 spray nozzlesto 36 spray nozzles, 36 spray nozzles to 39 spray nozzles, and 39 spraynozzles to 42 spray nozzles.

In embodiments, where 1 spray nozzles are used, the flow through eachspray nozzle in gallons per hour (GPH) ranges from one of more from thegroup consisting of: 30 GPH to 90 GPH, 90 GPH to 210 GPH, 210 GPH to 330GPH, 330 GPH to 450 GPH, and 450 GPH to 630 GPH. In embodiments, where 2spray nozzles are used, the flow through each spray nozzle ranges fromone of more from the group consisting of: 15 GPH to 45 GPH, 45 GPH to105 GPH, 105 GPH to 165 GPH, 165 GPH to 225 GPH, and 225 GPH to 315 GPH.In embodiments, where 3 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 10GPH to 30 GPH 30 GPH to 70 GPH 70 GPH to 110 GPH 110 GPH to 150 GPH, and150 GPH to 210 GPH.

In embodiments, where 4 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8 GPHto 23 GPH, 23 GPH to 53 GPH, 53 GPH to 83 GPH, 83 GPH to 113 GPH, and113 GPH to 158 GPH. In embodiments, where 5 spray nozzles are used, theflow through each spray nozzle ranges from one of more from the groupconsisting of: 6 GPH to 18 GPH, 18 GPH to 42 GPH, 42 GPH to 66 GPH, 66GPH to 90 GPH, and 90 GPH to 126 GPH. In embodiments, where 6 spraynozzles are used, the flow through each spray nozzle ranges from one ofmore from the group consisting of: 15 GPH to 35 GPH, 35 GPH to 55 GPH,55 GPH to 75 GPH, and 75 GPH to 105 GPH.

In embodiments, where 7 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of:12.857 GPH and 30 GPH, 30 GPH and 47.143 GPH, 47.143 GPH and 64.286 GPH,and 64.286 GPH and 90 GPH. In embodiments, where 8 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 11.250 GPH to 26.250 GPH, 26.250 GPH to 41.250GPH, 41.250 GPH to 56.250 GPH, and 56.250 GPH to 78.750 GPH. Inembodiments, where 9 spray nozzles are used, the flow through each spraynozzle ranges from one of more from the group consisting of: 10.000 GPHto 23.333 GPH, 23.333 GPH to 36.667 GPH, 36.667 GPH to 50.000 GPH, and50.000 GPH to 70.000 GPH.

In embodiments, where 10 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 9 GPHto 21 GPH, 21 GPH to 33 GPH, 33 GPH to 45 GPH, and 45 GPH to 63 GPH. Inembodiments, where 11 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8.182GPH to 19.091 GPH, 19.091 GPH to 30.000 GPH, 30.000 GPH to 40.909 GPH,and 40.909 GPH to 57.273 GPH. In embodiments, where 12 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 7.5 GPH to 17.5 GPH, 17.5 GPH to 27.5 GPH, 27.5GPH to 37.5 GPH, and 37.5 GPH to 52.5 GPH.

In embodiments, where 13 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.923GPH to 16.154 GPH, 16.154 GPH to 25.385 GPH, 25.385 GPH to 34.615 GPH,and 34.615 GPH to 48.462 GPH. In embodiments, where 14 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 6.429 GPH to 15.000 GPH, 15.000 GPH to 23.571GPH, 23.571 GPH to 32.143 GPH, and 32.143 GPH to 45.000 GPH. Inembodiments, where 15 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6 GPHto 14 GPH, 14 GPH to 22 GPH, 22 GPH to 30 GPH, and 30 GPH to 42 GPH.

In embodiments, where 16 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of:13.125 GPH to 20.625 GPH, 20.625 GPH to 28.125 GPH, and 28.125 GPH to39.375 GPH. In embodiments, where 17 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 12.353 GPH to 19.412 GPH, 19.412 GPH to 26.471 GPH, and26.471 GPH to 37.059 GPH. In embodiments, where 18 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 11.667 GPH to 18.333 GPH, 18.333 GPH to 25.000GPH, and 25.000 GPH to 35.000 GPH.

In embodiments, where 19 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of:11.053 GPH to 17.368 GPH, 17.368 GPH to 23.684 GPH, and 23.684 GPH to33.158 GPH. In embodiments, where 20 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 10.500 GPH to 16.500 GPH, 16.500 GPH to 22.500 GPH, and22.500 GPH to 31.500 GPH. In embodiments, where 21 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 10.000 GPH to 15.714 GPH, 15.714 GPH to 21.429GPH, and 21.429 GPH to 30.000 GPH.

In embodiments, where 22 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 9.545GPH to 15.000 GPH, 15.000 GPH to 20.455 GPH, and 20.455 GPH to 28.636GPH. In embodiments, where 23 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:9.130 GPH to 14.348 GPH, 14.348 GPH to 19.565 GPH, and 19.565 GPH to27.391 GPH. In embodiments, where 24 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 8.75 GPH to 13.75 GPH, 13.75 GPH to 18.75 GPH, and 18.75GPH to 26.25 GPH.

In embodiments, where 25 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8.40GPH to 13.20 GPH, 13.20 GPH to 18.00 GPH, and 18.00 GPH to 25.20 GPH. Inembodiments, where 26 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8.077GPH to 12.692 GPH, 12.692 GPH to 17.308 GPH, and 17.308 GPH to 24.231GPH. In embodiments, where 27 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:7.778 GPH to 12.222 GPH, 12.222 GPH to 16.667 GPH, and 16.667 GPH to23.333 GPH.

In embodiments, where 28 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 7.500GPH to 11.786 GPH, 11.786 GPH to 16.071 GPH, and 16.071 GPH to 22.500GPH. In embodiments, where 29 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:7.241 GPH to 11.379 GPH, 11.379 GPH to 15.517 GPH, and 15.517 GPH to21.724 GPH. In embodiments, where 30 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 7 GPH to 11 GPH, 11 GPH to 15 GPH, and 15 GPH to 21 GPH.

In embodiments, where 31 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.774GPH to 10.645 GPH, 10.645 GPH to 14.516 GPH, and 14.516 GPH to 20.323GPH. In embodiments, where 32 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:6.563 GPH to 10.313 GPH, 10.313 GPH to 14.063 GPH, and 14.063 GPH to19.688 GPH. In embodiments, where 33 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 6.364 GPH to 10.000 GPH, 10.000 GPH to 13.636 GPH, and13.636 GPH to 19.091 GPH.

In embodiments, where 34 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.176GPH to 9.706 GPH, 9.706 GPH to 13.235 GPH, and 13.235 GPH to 18.529 GPH.In embodiments, where 35 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.000GPH to 9.429 GPH, 9.429 GPH to 12.857 GPH, and 12.857 GPH to 18.000 GPH.In embodiments, where 36 spray nozzles are used, the flow through eachspray nozzle ranges from 9.167 GPH to 12.500 GPH, or 12.500 GPH to17.500 GPH. In embodiments, where 37 spray nozzles are used, the flowthrough each spray nozzle ranges from 8.919 GPH to 12.162 GPH, or 12.162GPH to 17.027 GPH. In embodiments, where 38 spray nozzles are used, theflow through each spray nozzle ranges from 8.684 GPH to 11.842 GPH, or11.842 GPH to 16.579 GPH. In embodiments, where 39 spray nozzles areused, the flow through each spray nozzle ranges from 8.462 GPH to 11.538GPH, or 11.538 GPH to 16.154 GPH. In embodiments, where 40 spray nozzlesare used, the flow through each spray nozzle ranges from 8.250 GPH to11.250 GPH, or 11.250 GPH to 15.750 GPH. In embodiments, where 41 spraynozzles are used, the flow through each spray nozzle ranges 8.049 GPH to10.976 GPH, or 10.976 GPH to 15.366 GPH. In embodiments, where 42 spraynozzles are used, the flow through each spray nozzle ranges from 7.857GPH to 10.714 GPH, or 10.714 GPH to 15.000 GPH.

In embodiments, the drying chamber (KBG) is equipped with a heatingjacket (KBJ), the heating jacket (KBJ) has a heat transfer medium inlet(KBK) and a heat transfer medium outlet (KBL). FIG. 14K shows theheating jacket (KBJ) installed over a portion of the drying chamber(KBG) creating an interior (KBJ1) having an annular space within which aheat transfer medium flows. A source of steam is provided to the heattransfer medium inlet (KBK). This steam may be a ninth steam supply(LDP) that is provided from a steam drum (LBE) as indicated on FIG. 14L.

In embodiments, a steam trap (KX6) is configured to accept steam,condensate, or non-condensable gases from the interior (KBJ1) of theheating jacket (KBJ) via a heat transfer medium outlet (KBL). Steam,condensate, or non-condensable gases are passed through the valve.During normal operation, only condensate flow through the steam trap(KX6). The condensate the flows through the steam trap (KX6) is theninth condensate (LJB) that is passed to the condensate tank (LAP) asshown on FIG. 14L.

In embodiments, the steam trap (KX6) is a valve which automaticallydrains the condensate from the interior (KBJ1) of the heating jacket(KBJ) while remaining tight to live steam, or if necessary, allowingsteam to flow at a controlled or adjusted rate. In embodiments, thesteam trap (KX6) also allows non-condensable gases to pass through itwhile remaining tight to steam. In embodiments, the steam trap (KX6) isa mechanical trap such as a bucket trap or a floating ball trap. Inembodiments, the steam trap (KX6) is a thermostatic trap such as abalanced pressure trap or a bimetallic trap. In embodiments, the steamtrap (KX6) is a thermodynamic trap which work by using the difference invelocity between steam and condensate.

In embodiments, a steam flow control valve (KX1) is provided and isconfigured to regulate the flow of steam that is passes through theheating jacket (KBJ). The steam flow control valve (KX1) has acontroller (KX2) which is configured to input or output a signal (KX3)to the computer (COMP). FIG. 14K shows the steam flow control valve(KX1) positioned to regulate steam that enters the heat transfer mediuminlet (KBK) of the heating jacket (KBJ). It is to be noted that it isalso contemplated that in certain instances, the steam flow controlvalve (KX1) may be positioned to regulate the heat transfer fluid thatis discharged from the interior (KBJ1) of the heating jacket (KBJ) viathe heat transfer medium outlet (KBL).

In embodiments, a flow sensor (KX4) is provided to measure the flow ofheat transfer fluid that is passes through the heating jacket (KBJ).FIG. 14K shows the flow sensor (KX4) positioned to measure the flow ofsteam that enters the heat transfer medium inlet (KBK) of the heatingjacket (KBJ). It is to be noted that it is also contemplated that incertain instances, the flow sensor (KX4) may be positioned to measurethe heat transfer fluid (steam or steam condensate) that is dischargedfrom the interior (KBJ1) of the heating jacket (KBJ) via the heattransfer medium outlet (KBL). The flow sensor (KX4) inputs a signal(KX5) to the computer (COMP).

In embodiment, the heating jacket (KBJ) is configured to maintain thewall (KWG) within the interior (KBG′) drying chamber (KBG) at a constanttemperature. In embodiments, the wall temperature ranges from one ormore from the group consisting of between: 110 degrees Fahrenheit to 125degrees Fahrenheit; 125 degrees Fahrenheit to 140 degrees Fahrenheit;140 degrees Fahrenheit to 155 degrees Fahrenheit; 155 degrees Fahrenheitto 170 degrees Fahrenheit; 170 degrees Fahrenheit to 185 degreesFahrenheit; 185 degrees Fahrenheit to 200 degrees Fahrenheit; 200degrees Fahrenheit to 215 degrees Fahrenheit; 215 degrees Fahrenheit to230 degrees Fahrenheit; 230 degrees Fahrenheit to 245 degreesFahrenheit; 250 degrees Fahrenheit to 275 degrees Fahrenheit; 275degrees Fahrenheit to 300 degrees Fahrenheit; 300 degrees Fahrenheit to325 degrees Fahrenheit; 325 degrees Fahrenheit to 350 degreesFahrenheit; 350 degrees Fahrenheit to 375 degrees Fahrenheit; 375degrees Fahrenheit to 400 degrees Fahrenheit; 400 degrees Fahrenheit to425 degrees Fahrenheit; 425 degrees Fahrenheit to 450 degreesFahrenheit; 450 degrees Fahrenheit to 475 degrees Fahrenheit; 475degrees Fahrenheit to 500 degrees Fahrenheit; 500 degrees Fahrenheit to525 degrees Fahrenheit; 525 degrees Fahrenheit to 550 degreesFahrenheit; 550 degrees Fahrenheit to 575 degrees Fahrenheit; 575degrees Fahrenheit to 600 degrees Fahrenheit; 600 degrees Fahrenheit to625 degrees Fahrenheit; 625 degrees Fahrenheit to 650 degreesFahrenheit; 650 degrees Fahrenheit to 675 degrees Fahrenheit; 675degrees Fahrenheit to 700 degrees Fahrenheit; 700 degrees Fahrenheit to725 degrees Fahrenheit; 725 degrees Fahrenheit to 750 degreesFahrenheit; 750 degrees Fahrenheit to 775 degrees Fahrenheit; and 775degrees Fahrenheit to 800 degrees Fahrenheit.

In embodiments, it is desired to operate the heating jacket (KBJ) tomaintain a wall (KWG) temperature sufficient to avoid sticking,deposition, burning of insect particulates or liquid upon surface of thewall (KWG). In embodiments, the surface of the wall (KWG) transfers heatinto the interior (KBG) of the drying chamber (KBG). In embodiments, itis desired to operate the heating jacket (KBJ) in a manner that issufficient to maintain a wall (KWG) temperature that is known to nowfouling of the heat surface by sticking, deposition, burning of insectparticulates or liquid upon surface of the wall (KWG). Powder build-upon the wall (KWG) within the interior (KBG′) surface of the dryingchamber (KBG) poses problems related to start-up and shutdown asdiscussed below.

In embodiments, the openings (KM4) of the screen (KM3) or mesh (KM3′)are selected from one or more from the group consisting of 1680 micronsto 2000 microns, 1410 microns to 1680 microns, 1190 microns to 1410microns, 1000 microns to 1190 microns, 841 microns to 1000 microns, 707microns to 841 microns, 595 microns to 707 microns, 500 microns to 595microns, 400 microns to 500 microns, 354 microns to 400 microns, 297microns to 354 microns, 250 microns to 297 microns, 210 microns to 250microns, 177 microns to 210 microns, 149 microns to 177 microns, 125microns to 149 microns, 105 microns to 125 microns, 88 microns to 105microns, 74 microns to 88 microns, 63 microns to 74 microns, and 53microns to 63 microns.

In embodiments, the temperature sensor (KBY) positioned on the firsttransfer conduit (KBW) in between the second output (KBU) of the spraydryer (KAP) and the first input (KCB) of the first separator (KCA) thatmeasures the temperature of the insect and gas mixture (KBV) ispreferably optimized to be maintained at 120 degrees Fahrenheit to 400degrees Fahrenheit, or between 135 degrees Fahrenheit to 300 degreesFahrenheit, or between 140 degrees Fahrenheit to 160 degrees Fahrenheit,or between 146 degrees Fahrenheit to 154 degrees Fahrenheit. Thetemperature sensor (KBY) inputs a signal (KBX) to the computer (COMP).

In embodiments, the temperature sensor (KBY) positioned on the firsttransfer conduit (KBW) in between the second output (KBU) of the spraydryer (KAP) and the first input (KCB) of the first separator (KCA) thatmeasures the temperature of the insect and gas mixture (KBV) ispreferably optimized to be maintained at 150 degrees Fahrenheit to 250degrees Fahrenheit, but more preferably to 135 degrees Fahrenheit to 180degrees Fahrenheit, but more preferably to 145 degrees Fahrenheit to 155degrees Fahrenheit.

In embodiments, the temperature of the insect and gas mixture (KBV)leaving the drying chamber (KBG) ranges from one or more from the groupconsisting of between: 110 degrees Fahrenheit to 125 degrees Fahrenheit;125 degrees Fahrenheit to 140 degrees Fahrenheit; 140 degrees Fahrenheitto 155 degrees Fahrenheit; 155 degrees Fahrenheit to 170 degreesFahrenheit; 170 degrees Fahrenheit to 185 degrees Fahrenheit; 185degrees Fahrenheit to 200 degrees Fahrenheit; 200 degrees Fahrenheit to215 degrees Fahrenheit; 215 degrees Fahrenheit to 230 degreesFahrenheit; 230 degrees Fahrenheit to 245 degrees Fahrenheit; 250degrees Fahrenheit to 275 degrees Fahrenheit; 275 degrees Fahrenheit to300 degrees Fahrenheit; 300 degrees Fahrenheit to 325 degreesFahrenheit; 325 degrees Fahrenheit to 350 degrees Fahrenheit; 350degrees Fahrenheit to 375 degrees Fahrenheit; and 375 degrees Fahrenheitto 400 degrees Fahrenheit.

In embodiments, the difference in temperature between the heated gassupply (KAG′) and the insect and gas mixture (KBV) ranges from between110 degrees Fahrenheit to 125 degrees Fahrenheit; 125 degrees Fahrenheitto 140 degrees Fahrenheit; 140 degrees Fahrenheit to 155 degreesFahrenheit; 155 degrees Fahrenheit to 170 degrees Fahrenheit; 170degrees Fahrenheit to 185 degrees Fahrenheit; 185 degrees Fahrenheit to200 degrees Fahrenheit; 200 degrees Fahrenheit to 215 degreesFahrenheit; 215 degrees Fahrenheit to 230 degrees Fahrenheit; 230degrees Fahrenheit to 245 degrees Fahrenheit; 250 degrees Fahrenheit to275 degrees Fahrenheit; 275 degrees Fahrenheit to 300 degreesFahrenheit; 300 degrees Fahrenheit to 325 degrees Fahrenheit; 325degrees Fahrenheit to 350 degrees Fahrenheit; 350 degrees Fahrenheit to375 degrees Fahrenheit; 375 degrees Fahrenheit to 400 degreesFahrenheit; 400 degrees Fahrenheit to 425 degrees Fahrenheit; 425degrees Fahrenheit to 450 degrees Fahrenheit; 450 degrees Fahrenheit to475 degrees Fahrenheit; 475 degrees Fahrenheit to 500 degreesFahrenheit.

In embodiments, a pressure sensor (KBH) is configured to measure thepressure within the interior (KBG′) of the drying chamber (KBG) andoutput a signal (KBI) to the computer (COMP). In embodiments, the rangesof pressure within the interior (KBG′) of the drying chamber (KBG) isselected from one of more from the group consisting of: 1.5 pounds persquare inch absolute (PSIA) 3 PSIA, 3 PSIA to 4.5 PSIA, 4.5 PSIA to 6PSIA, 6 PSIA to 7.5 PSIA, 7.5 PSIA to 9 PSIA, 9 PSIA to 10.5 PSIA, 10.5PSIA to 12 PSIA, 12 PSIA to 13.5 PSIA, 12 PSIA to 12.25 PSIA, 12.25 PSIAto 12.5 PSIA, 12.5 PSIA to 12.75 PSIA, 12.75 PSIA to 13 PSIA, 13 PSIA to13.25 PSIA, 13.25 PSIA to 13.5 PSIA, 13.5 PSIA to 13.75 PSIA, 13.75 PSIAto 14 PSIA, 14 PSIA to 14.25 PSIA, 14.25 PSIA to 14.5 PSIA, 14.5 PSIA to14.75 PSIA, 14.75 PSIA to 15 PSIA, 15 PSIA to 16.5 PSIA, 16.5 PSIA to 18PSIA, 18 PSIA to 19.5 PSIA, 19.5 PSIA to 21 PSIA, 21 PSIA to 22.5 PSIA,22.5 PSIA to 24 PSIA, 24 PSIA to 25.5 PSIA, 25.5 PSIA to 27 PSIA, 27PSIA to 28.5 PSIA, 28.5 PSIA to 30 PSIA, 30 PSIA to 31.5 PSIA, 31.5 PSIAto 33 PSIA, 33 PSIA to 34.5 PSIA, and 34.5 PSIA to 36 PSIA.

In embodiments, the ranges of pressure within the interior (KBG′) of thedrying chamber (KBG) is selected from one of more from the groupconsisting of: between about 0.001 inches of water to about 0.002 inchesof water; between about 0.002 inches of water to about 0.003 inches ofwater; between about 0.003 inches of water to about 0.006 inches ofwater; between about 0.006 inches of water to about 0.012 inches ofwater; between about 0.012 inches of water to about 0.024 inches ofwater; between about 0.024 inches of water to about 0.050 inches ofwater; between about 0.050 inches of water to about 0.075 inches ofwater; between about 0.075 inches of water to about 0.150 inches ofwater; between about 0.150 inches of water to about 0.300 inches ofwater; between about 0.300 inches of water to about 0.450 inches ofwater; between about 0.450 inches of water to about 0.473 inches ofwater; between about 0.473 inches of water to about 0.496 inches ofwater; between about 0.496 inches of water to about 0.521 inches ofwater; between about 0.521 inches of water to about 0.547 inches ofwater; between about 0.547 inches of water to about 0.574 inches ofwater; between about 0.574 inches of water to about 0.603 inches ofwater; between about 0.603 inches of water to about 0.633 inches ofwater; between about 0.633 inches of water to about 0.665 inches ofwater; between about 0.665 inches of water to about 0.698 inches ofwater; between about 0.698 inches of water to about 0.733 inches ofwater; between about 0.733 inches of water to about 0.770 inches ofwater; between about 0.770 inches of water to about 0.808 inches ofwater; between about 0.808 inches of water to about 0.849 inches ofwater; between about 0.849 inches of water to about 0.891 inches ofwater; between about 0.891 inches of water to about 0.936 inches ofwater; between about 0.936 inches of water to about 0.982 inches ofwater; between about 0.982 inches of water to about 1.031 inches ofwater; between about 1.031 inches of water to about 1.083 inches ofwater; between about 1.083 inches of water to about 1.137 inches ofwater; between about 1.137 inches of water to about 1.194 inches ofwater; between about 1.194 inches of water to about 1.254 inches ofwater; between about 1.254 inches of water to about 1.316 inches ofwater; between about 1.316 inches of water to about 1.382 inches ofwater; between about 1.382 inches of water to about 1.451 inches ofwater; between about 1.451 inches of water to about 1.524 inches ofwater; between about 1.524 inches of water to about 2.286 inches ofwater; between about 2.286 inches of water to about 3.429 inches ofwater; between about 3.429 inches of water to about 5.143 inches ofwater; between about 5.143 inches of water to about 7.715 inches ofwater; between about 7.715 inches of water to about 11.572 inches ofwater; between about 11.572 inches of water to about 17.358 inches ofwater; between about 17.358 inches of water to about 26.037 inches ofwater; between about 26.037 inches of water to about 39.055 inches ofwater; between about 39.055 inches of water to about 58.582 inches ofwater; between about 58.582 inches of water to about 87.873 inches ofwater; between about 87.873 inches of water to about 131.810 inches ofwater; between about 131.810 inches of water to about 197.715 inches ofwater; between about 197.715 inches of water to about 296.573 inches ofwater; or, between about 296.573 inches of water to about 400 inches ofwater.

Spray dried insects (KBT) may be removed from the first output (KB S) ofthe drying chamber (KBG). In embodiments, the insects (KBT) removed fromthe first output (KBS) of the drying chamber (KBG) may be solid or maycontain liquid. In embodiments, the insects (KBT) removed from the firstoutput (KB S) of the drying chamber (KBG) are either too wet or toolarge, or both, to be evacuated from the second output (KBU) of thedrying chamber (KBG). In embodiments, the insects (KBT) removed from thefirst output (KB S) of the drying chamber (KBG) are routed to the mixingtank (G15) on FIG. 14G or to the interior (6A3) insect tank (6A2) ofFIG. 14K. In embodiments, the insects (KBT) removed from the firstoutput (KB S) may be mixed with one or more stream of separated insects,such first separated insects (KCG), second separated insects (KCP),third separated insects (KCV), a fourth separated insects (KCX), or alarge insect particulate portion (KCY) to form combined insects (KM7) asshown in FIG. 14K.

In embodiments, the vibrator (KBN) is connected to the spray dryer (KAP)or drying chamber (KBG) via a connection (KBR). In embodiments, thespray dryer (KAP) or drying chamber (KBG) is equipped with a vibrator(KBN). In embodiments, a vibrator (KBN) vibrates at least a portion ofthe spray dryer (KAP) or drying chamber (KBG) to aide in removal of thespray dried insects (KBT) from the first output (KBS). In embodiments,the vibrator (KBN) is pneumatic. In embodiments, the vibrator (KBN)operates at a vibration range that is selected from one or more from thegroup consisting of 3,000 vibrations per minute (VPM) to 4000 VPM, 4,000VPM to 5,000 VPM, 5,000 VPM to 5,500 VPM, 5,500 VPM to 6,000 VPM, 6,000VPM to 6,500 VPM, 6,500 VPM to 7,000 VPM, 7,000 VPM to 7,500 VPM, 7,500VPM to 8,000 VPM, 8,000 VPM to 8,500 VPM, 8,500 VPM to 9,000 VPM, 9,000VPM to 9,500 VPM, 9,500 VPM to 10,000 VPM, 10,000 VPM to 15,000 VPM,15,000 VPM to 20,000 VPM, 20,000 VPM to 25,000 VPM, 25,000 VPM to 30,000VPM, 30,000 VPM to 35,000 VPM, 35,000 VPM to 40,000 VPM, 40,000 VPM to45,000 VPM, and 45,000 VPM to 50,000 VPM. In embodiments, the vibrator(KBN) has a motor (KBO) with a controller (KBP) that is configured toinput or output a signal (KBQ) to the computer (COMP).

In embodiments, the small insect particulate portion (KCW) has a watercontent that ranges from one or more from the group selected from 0.05weight percent of water to 0.1 weight percent of water, 0.1 weightpercent of water to 0.2 weight percent of water, 0.2 weight percent ofwater to 0.4 weight percent of water, 0.4 weight percent of water to 0.8weight percent of water, 0.8 weight percent of water to 1 weight percentof water, 1 weight percent of water to 2 weight percent of water, 2weight percent of water to 3 weight percent of water, 3 weight percentof water to 4 weight percent of water, 4 weight percent of water to 5weight percent of water, 5 weight percent of water to 6 weight percentof water, 6 weight percent of water to 7 weight percent of water, 7weight percent of water to 8 weight percent of water, 8 weight percentof water to 9 weight percent of water, 9 weight percent of water to 10weight percent of water, 10 weight percent of water to 11 weight percentof water, 11 weight percent of water to 12 weight percent of water, 12weight percent of water to 13 weight percent of water, 13 weight percentof water to 14 weight percent of water, 14 weight percent of water to 15weight percent of water, 15 weight percent of water to 16 weight percentof water, 16 weight percent of water to 17 weight percent of water, 17weight percent of water to 18 weight percent of water, 18 weight percentof water to 19 weight percent of water, and 19 weight percent of waterto 20 weight percent of water.

In embodiments, the small insect particulate portion (KCW) has a liquidcontent that ranges from one or more from the group selected from 0.05weight percent of liquid to 0.1 weight percent of liquid, 0.1 weightpercent of liquid to 0.2 weight percent of liquid, 0.2 weight percent ofliquid to 0.4 weight percent of liquid, 0.4 weight percent of liquid to0.8 weight percent of liquid, 0.8 weight percent of liquid to 1 weightpercent of liquid, 1 weight percent of liquid to 2 weight percent ofliquid, 2 weight percent of liquid to 3 weight percent of liquid, 3weight percent of liquid to 4 weight percent of liquid, 4 weight percentof liquid to 5 weight percent of liquid, 5 weight percent of liquid to 6weight percent of liquid, 6 weight percent of liquid to 7 weight percentof liquid, 7 weight percent of liquid to 8 weight percent of liquid, 8weight percent of liquid to 9 weight percent of liquid, 9 weight percentof liquid to 10 weight percent of liquid, 10 weight percent of liquid to11 weight percent of liquid, 11 weight percent of liquid to 12 weightpercent of liquid, 12 weight percent of liquid to 13 weight percent ofliquid, 13 weight percent of liquid to 14 weight percent of liquid, 14weight percent of liquid to 15 weight percent of liquid, 15 weightpercent of liquid to 16 weight percent of liquid, 16 weight percent ofliquid to 17 weight percent of liquid, 17 weight percent of liquid to 18weight percent of liquid, 18 weight percent of liquid to 19 weightpercent of liquid, and 19 weight percent of liquid to 20 weight percentof liquid.

In embodiments, the large insect particulate portion (KCY) has a watercontent that ranges from one or more from the group selected from 0.05weight percent of water to 0.1 weight percent of water, 0.1 weightpercent of water to 0.2 weight percent of water, 0.2 weight percent ofwater to 0.4 weight percent of water, 0.4 weight percent of water to 0.8weight percent of water, 0.8 weight percent of water to 1 weight percentof water, 1 weight percent of water to 2 weight percent of water, 2weight percent of water to 3 weight percent of water, 3 weight percentof water to 4 weight percent of water, 4 weight percent of water to 5weight percent of water, 5 weight percent of water to 6 weight percentof water, 6 weight percent of water to 7 weight percent of water, 7weight percent of water to 8 weight percent of water, 8 weight percentof water to 9 weight percent of water, 9 weight percent of water to 10weight percent of water, 10 weight percent of water to 11 weight percentof water, 11 weight percent of water to 12 weight percent of water, 12weight percent of water to 13 weight percent of water, 13 weight percentof water to 14 weight percent of water, 14 weight percent of water to 15weight percent of water, 15 weight percent of water to 16 weight percentof water, 16 weight percent of water to 17 weight percent of water, 17weight percent of water to 18 weight percent of water, 18 weight percentof water to 19 weight percent of water, and 19 weight percent of waterto 20 weight percent of water.

In embodiments, the large insect particulate portion (KCY) has a liquidcontent that ranges from one or more from the group selected from 0.05weight percent of liquid to 0.1 weight percent of liquid, 0.1 weightpercent of liquid to 0.2 weight percent of liquid, 0.2 weight percent ofliquid to 0.4 weight percent of liquid, 0.4 weight percent of liquid to0.8 weight percent of liquid, 0.8 weight percent of liquid to 1 weightpercent of liquid, 1 weight percent of liquid to 2 weight percent ofliquid, 2 weight percent of liquid to 3 weight percent of liquid, 3weight percent of liquid to 4 weight percent of liquid, 4 weight percentof liquid to 5 weight percent of liquid, 5 weight percent of liquid to 6weight percent of liquid, 6 weight percent of liquid to 7 weight percentof liquid, 7 weight percent of liquid to 8 weight percent of liquid, 8weight percent of liquid to 9 weight percent of liquid, 9 weight percentof liquid to 10 weight percent of liquid, 10 weight percent of liquid to11 weight percent of liquid, 11 weight percent of liquid to 12 weightpercent of liquid, 12 weight percent of liquid to 13 weight percent ofliquid, 13 weight percent of liquid to 14 weight percent of liquid, 14weight percent of liquid to 15 weight percent of liquid, 15 weightpercent of liquid to 16 weight percent of liquid, 16 weight percent ofliquid to 17 weight percent of liquid, 17 weight percent of liquid to 18weight percent of liquid, 18 weight percent of liquid to 19 weightpercent of liquid, and 19 weight percent of liquid to 20 weight percentof liquid.

In embodiments, the insects (KBT) removed the drying chamber (KBG) havea water content that ranges from one or more from the group selectedfrom 0.05 weight percent of water to 0.1 weight percent of water, 0.1weight percent of water to 0.2 weight percent of water, 0.2 weightpercent of water to 0.4 weight percent of water, 0.4 weight percent ofwater to 0.8 weight percent of water, 0.8 weight percent of water to 1weight percent of water, 1 weight percent of water to 2 weight percentof water, 2 weight percent of water to 3 weight percent of water, 3weight percent of water to 4 weight percent of water, 4 weight percentof water to 5 weight percent of water, 5 weight percent of water to 6weight percent of water, 6 weight percent of water to 7 weight percentof water, 7 weight percent of water to 8 weight percent of water, 8weight percent of water to 9 weight percent of water, 9 weight percentof water to 10 weight percent of water, 10 weight percent of water to 11weight percent of water, 11 weight percent of water to 12 weight percentof water, 12 weight percent of water to 13 weight percent of water, 13weight percent of water to 14 weight percent of water, 14 weight percentof water to 15 weight percent of water, 15 weight percent of water to 16weight percent of water, 16 weight percent of water to 17 weight percentof water, 17 weight percent of water to 18 weight percent of water, 18weight percent of water to 19 weight percent of water, and 19 weightpercent of water to 20 weight percent of water.

In embodiments, the insects (KBT) removed the drying chamber (KBG) havea liquid content that ranges from one or more from the group selectedfrom 0.05 weight percent of liquid to 0.1 weight percent of liquid, 0.1weight percent of liquid to 0.2 weight percent of liquid, 0.2 weightpercent of liquid to 0.4 weight percent of liquid, 0.4 weight percent ofliquid to 0.8 weight percent of liquid, 0.8 weight percent of liquid to1 weight percent of liquid, 1 weight percent of liquid to 2 weightpercent of liquid, 2 weight percent of liquid to 3 weight percent ofliquid, 3 weight percent of liquid to 4 weight percent of liquid, 4weight percent of liquid to 5 weight percent of liquid, 5 weight percentof liquid to 6 weight percent of liquid, 6 weight percent of liquid to 7weight percent of liquid, 7 weight percent of liquid to 8 weight percentof liquid, 8 weight percent of liquid to 9 weight percent of liquid, 9weight percent of liquid to 10 weight percent of liquid, 10 weightpercent of liquid to 11 weight percent of liquid, 11 weight percent ofliquid to 12 weight percent of liquid, 12 weight percent of liquid to 13weight percent of liquid, 13 weight percent of liquid to 14 weightpercent of liquid, 14 weight percent of liquid to 15 weight percent ofliquid, 15 weight percent of liquid to 16 weight percent of liquid, 16weight percent of liquid to 17 weight percent of liquid, 17 weightpercent of liquid to 18 weight percent of liquid, 18 weight percent ofliquid to 19 weight percent of liquid, and 19 weight percent of liquidto 20 weight percent of liquid.

In embodiments, the spray dryer (KAP) drying chamber (KBG) is configuredto mix the heated gas supply (KAG′) with the insect liquid mixture (H39,KAS) to form an insect and gas mixture (KBV). The insect and gas mixture(KBV) is discharged from the spray dryer (KAP) via a second output(KBU). The insect and gas mixture (KBV) include a spray dried insectportion (KBV′), a vapor portion (KBV″), and a gas portion (KBV′″). Inembodiments, the spray dried insect portion (KBV′) may include solidparticulates. In embodiments, the vapor portion (KBV″) is steam. Inembodiments, the vapor portion (KBV″) may include the vapor-phase of theliquid within the insect liquid mixture (H39, KAS) which may includewater. In other embodiments, the vapor portion (KBV″) may include thevapor-phase of the liquid within the insect liquid mixture (H39, KAS)which may include an acid, alcohol, diglycerides, esters, ethanol,butanol, n-butanol, sec-butanol, isobutanol, tert-butanol, ethylacetate, glycerin, glycerol, hexane, hydrocarbon, insect lipids,isopropyl alcohol, methanol, Monoglycerides, oil, and solvent. Inembodiments, the gas portion (KBV″) includes whatever was within the gassupply (KAG).

The spray dryer (KAP) has a second output (KBU) that is configured todischarge an insect and gas mixture (KBV) from the interior (KBG′) ofthe drying chamber (KBG). In embodiments, the insect and gas mixture(KBV) has a spray dried insect portion (KBV′), vapor portion (KBV″), anda gas portion (KBV′″). The second output (KBU) of the spray dryer (KAP)is connected to the first-first input (KCB) of the first separator (KCA)via a first transfer conduit (KBW). In embodiments, the first separator(KCA) is a cyclone or a filter. FIG. 14K shows the first separator (KCA)as a cyclone.

The first transfer conduit (KBW) transfers the insect and gas mixture(KBV) from the interior (KBG′) of the drying chamber (KBG) to the firstseparator (KCA). The first separator (KCA) separates first separatedinsects (KCG) from the insect and gas mixture (KBV) to create a firstinsect depleted gas stream (KCD). The first insect depleted gas stream(KCD) is discharged from the first separator (KCA) via a first-firstoutput (KCC).

The first separator (KCA) has: a first-first input (KCB) for receivingthe insect and gas mixture (KBV) from the spray dryer (KAP), afirst-first output (KCC) for evacuating the first insect depleted gasstream (KCD) towards the second separator (KCI), and a first-secondoutput (KCF) for transferring first separated insects (KCG) towards thethird separator (KCR). The first insect depleted gas stream (KCD) istransferred from the first-first output (KCC) to the second-first input(KCK) of the second separator (KCI) via a second transfer conduit (KCE).

The first insect depleted gas stream (KCD) has a reduced amount ofinsects relative to the insect and gas mixture (KBV). The first insectdepleted gas stream (KCD) has a reduced amount of spray dried insectportion (KBV′) relative to the insect and gas mixture (KBV). The secondtransfer conduit (KCE) is connected at one end to the first-first output(KCC) of the first separator (KCA) and at another end to thesecond-first input (KCK) of the second separator (KCI).

The first separated insects (KCG) that are separated from the insect andgas mixture (KBV) are discharged from the first separator (KCA) via thefirst-second output (KCF). The third-first input (KCS) of the thirdseparator (KCR) is configured to receive the first separated insects(KCG) via a first dipleg (KCH). The first dipleg (KCH) is connected atone end to the first-second output (KCF) of the first separator (KCA)and at a second end to the third-first input (KCS) of the thirdseparator (KCR). The first separated insects (KCG) includes at least aportion of the spray dried insect portion (KBV′) that were separatedfrom the insect and gas mixture (KBV).

The second separator (KCI) separates second separated insects (KCP) fromthe first insect depleted gas stream (KCD) to create a second insectdepleted gas stream (KCM). The second insect depleted gas stream (KCM)has a reduced amount of insects relative to the first insect depletedgas stream (KCD). The second insect depleted gas stream (KCM) has areduced amount of spray dried insect portion (KBV′) relative to thefirst insect depleted gas stream (KCD).

In embodiments, the second separator (KCI) is a cyclone or a filter.FIG. 14K shows the second separator (KCI) as a cyclone. The secondinsect depleted gas stream (KCM) is discharged from the second separator(KCI) via a second-first output (KCJ).

The second separator (KCI) has: a second-first input (KCK) for receivingthe first insect depleted gas stream (KCD) from the first separator(KCA), a second-first output (KCJ) for evacuating the second insectdepleted gas stream (KCM) towards the fourth separator (KCZ), and asecond-second output (KCO) for transferring second separated insects(KCP) towards the third separator (KCR). The second insect depleted gasstream (KCM) is transferred from the second-first output (KCJ) to thefourth-first input (KDA) of the fourth separator (KCZ) via a thirdtransfer conduit (KCN). The third transfer conduit (KCN) is connected atone end to the second-first output (KCJ) of the second separator (KCI)and at another end to the fourth-first input (KDA) of the fourthseparator (KCZ).

The second separated insects (KCP) that are separated from the firstinsect depleted gas stream (KCD) are discharged from the secondseparator (KCI) via the second-second output (KCO). The third-firstinput (KCS) of the third separator (KCR) is configured to receive thesecond separated insects (KCP) via a second dipleg (KCQ). The seconddipleg (KCQ) is connected at one end to the second-second output (KCO)of the second separator (KCI) and at a second end to the third-firstinput (KCS) of the third separator (KCR). The second separated insects(KCP) includes at least a portion of the insects that were separatedfrom the first insect depleted gas stream (KCD). The second separatedinsects (KCP) includes at least a portion of the spray dried insectportion (KBV′) that were separated from the first insect depleted gasstream (KCD).

The fourth separator (KCZ) separates an additional separated insects(KDF) from the second insect depleted gas stream (KCM) to create a thirdinsect depleted gas stream (KDC). The third insect depleted gas stream(KDC) has a reduced amount of insects relative to the second insectdepleted gas stream (KCM). The third insect depleted gas stream (KDC)has a reduced amount of spray dried insect portion (KBV′) relative tothe second insect depleted gas stream (KCM). In embodiments, the fourthseparator (KCZ) is a cyclone, filter, scrubber, or electrostaticprecipitator.

FIG. 14K shows the second separator (KCI) as an electrostaticprecipitator. The electrostatic precipitator has an electrode (KM8) anda power supply (KM9) and is configured to separate insects from thesecond insect depleted gas stream (KCM). The electrode (KM8) and a powersupply (KM9) apply an electrostatic charge to the second insect depletedgas stream (KCM) as it passes through the fourth separator (KCZ).

In other embodiments, the fourth separator (KCZ) is a scrubber. Thescrubber, is preferably a vertically oriented cylindrical, orrectangular, pressure vessel having a lower section, and an uppersection, along with a central section that contains a quantity of packedmedia either comprising raschig rings, pall rings, berl saddles, intaloxpacking, metal structured grid packing, hollow spherical packing, highperformance thermoplastic packing, structured packing, synthetic wovenfabric, or ceramic packing, or the like, wherein media is supported upona suitable support grid system commonplace to industrial chemicalequipment systems. The upper section of the scrubber preferably containsa demister to enhance the removal of liquid droplets entrained in avapor stream and to minimize carry-over losses of the sorption liquid.This demister is also positioned above the scrubber spray nozzle system,comprised of a plurality of spray nozzles, or spray balls, thatintroduce and substantially equally distribute the scrubbing absorptionliquid to the scrubber onto the scrubber's central packing section, soit may gravity-flow down through the scrubber central section.

As the second insect depleted gas stream (KCM) passes up through theinternal packing of the scrubber, excess steam within the additionalseparated insects (KDF) comes into intimate contact with water and/or asolvent, which are cooled prior to being introduced to the upper sectionof the scrubber through the scrubber spray nozzle system. Steam fromwithin the second insect depleted gas stream (KCM) is condensed into aliquid.

The third insect depleted gas stream (KDC) is discharged from the fourthseparator (KCZ) via a fourth-first input (KDA). The fourth separator(KCZ) has: fourth-first input (KDA) for receiving the second insectdepleted gas stream (KCM) from the second separator (KCI), afourth-first output (KDB) for evacuating the third insect depleted gasstream (KDC) towards the condenser (KDH), and a fourth-second output(KDE) for transferring additional separated insects (KDF) towards thethird separator (KCR).

The third insect depleted gas stream (KDC) is transferred from thefourth-first output (KDB) to the gas-vapor inlet (KDP) of the condenser(KDH) via a fourth transfer conduit (KDD). The fourth transfer conduit(KDD) is connected at one end to the fourth-second output (KDE) of thefourth separator (KCZ) and at another end to the gas-vapor inlet (KDP)of the condenser (KDH). The additional separated insects (KDF) that areseparated from the second insect depleted gas stream (KCM) aredischarged from the fourth separator (KCZ) via the fourth-second output(KDE). In embodiments, the third-first input (KCS) of the thirdseparator (KCR) is configured to receive at least a portion of theadditional separated insects (KDF) via a fifth transfer conduit (KDG).The fifth transfer conduit (KDG) is connected at one end to thefourth-second output (KDE) of the fourth separator (KCZ) and at a secondend to the third-first input (KCS) of the third separator (KCR).

The third insect depleted gas stream (KDC) includes at least a portionof the vapor portion (KBV″) or gas portion (KBV″) of the insect and gasmixture (KBV) that was discharged from the drying chamber (KBG). Theadditional separated insects (KDF) includes at least a portion of theinsects that were separated from the first insect depleted gas stream(KCD). The additional separated insects (KDF) include at least a portionof the insects that were separated from the second insect depleted gasstream (KCM). The additional separated insects (KDF) includes at least aportion of the spray dried insect portion (KBV′) that were separatedfrom the second insect depleted gas stream (KCM).

In embodiments, the additional separated insects (KDF) have a size rangethat is selected from one or more from the group consisting of 0.001nanometers to 0.1 nanometers, 0.1 nanometers to 0.5 nanometers, 0.5nanometers to 1 nanometer, 1 nanometer to 5 nanometers, 5 nanometers to10 nanometers, 10 nanometers to 15 nanometers, 15 nanometers to 20nanometers, 20 nanometers to 25 nanometers, 25 nanometers to 30nanometers, 30 nanometers to 35 nanometers, 35 nanometers to 40nanometers, 40 nanometers to 45 nanometers, 45 nanometers to 50nanometers, 50 nanometers to 55 nanometers, 55 nanometers to 60nanometers, 60 nanometers to 65 nanometers, 65 nanometers to 70nanometers, 70 nanometers to 75 nanometers, 75 nanometers to 80nanometers, 80 nanometers to 85 nanometers, 85 nanometers to 90nanometers, 90 nanometers to 95 nanometers, 95 nanometers to 100nanometers, 100 nanometers to 200 nanometers, 200 nanometers to 300nanometers, 300 nanometers to 400 nanometers, 400 nanometers to 500nanometers, 500 nanometers to 600 nanometers, 600 nanometers to 700nanometers, 700 nanometers to 800 nanometers, and 800 nanometers to 900nanometers.

In embodiments, the additional separated insects (KDF) have a particlesize distribution (PSD) that has a lesser or smaller PSD relative to thesmall insect particulate portion (KCW) separated in the solid-solidseparator (SSS). In embodiments, the additional separated insects (KDF)have a particle size distribution (PSD) that has a lesser or smaller PSDrelative to the large insect particulate portion (KCY) separated in thesolid-solid separator (SSS). In embodiments, the particle sizedistribution of the small insect particulate portion (KCW) is lesser orsmaller than the particle size distribution of the large insectparticulate portion (KCY).

In embodiments, the small insect particulate portion (KCW) have a sizerange that is selected from one or more from the group consisting of 1microns to 5 microns, 5 microns to 10 microns, 10 microns to 30 microns,30 microns to 50 microns, 50 microns to 70 microns, 70 microns to 90microns, 90 microns to 110 microns, 110 microns to 130 microns, 130microns to 150 microns, 150 microns to 170 microns, 170 microns to 190microns, 190 microns to 210 microns, 210 microns to 230 microns, and 230microns to 250 microns.

In embodiments, the large insect particulate portion (KCY) have a sizerange that is selected from one or more from the group consisting of 50microns to 60 microns, 60 microns to 70 microns, 70 microns to 80microns, 80 microns to 90 microns, 90 microns to 100 microns, 100microns to 150 microns, 150 microns to 200 microns, 200 microns to 250microns, 250 microns to 300 microns, 300 microns to 350 microns, 350microns to 400 microns, 400 microns to 450 microns, 450 microns to 500microns, 500 microns to 550 microns, 550 microns to 600 microns, 600microns to 650 microns, 650 microns to 700 microns, 700 microns to 750microns, 750 microns to 800 microns, 800 microns to 850 microns, 850microns to 900 microns, 900 microns to 950 microns, and 950 microns to1,000 microns.

As shown in FIG. 14K the third separator (KCR) accepts first separatedinsects (KCG) from the first separator (KCA), and second separatedinsects (KCP) from the second separator (KCI), and optionally a portionof the additional separated insects (KDF) from the fourth separator(KCZ), and separates at least a small insect particulate portion (KCW)and a large insect particulate portion (KCY) therefrom. In embodiments,the small insect particulate portion (KCW) and a large insectparticulate portion (KCY) are oligosaccharides or arehydrolyzed-biopolymers, as discussed above.

In embodiments, the third separator (KCR) includes solid-solid separator(SSS). In embodiments, the third separator (KCR) includes a sifter asshown in FIG. 14K. In embodiments, the third separator (KCR) includes afilter. In embodiments, the third separator (KCR) has a third-firstinput (KCS) for receiving: first separated insects (KCG) via the firstdipleg (KCH), second separated insects (KCP) via the second dipleg(KCQ), and additional separated insects (KDF) via the fifth transferconduit (KDG). In embodiments, the third separator (KCR) has athird-first output (KCT) for discharging a third separated insects (KCV)which include a small insect particulate portion (KCW). In embodiments,the small insect particulate portion (KCW) may be transferred to themultifunctional composition tank (6F1) on FIG. 14A, mixing tank (C15) onFIG. 14C, or to the interior (6A3) insect tank (6A2) of FIG. 14K.

In embodiments, the third separator (KCR) has a third-second output(KCU) for discharging a fourth separated insects (KCX) which include alarge insect particulate portion (KCY). In embodiments, the large insectparticulate portion (KCY) may be transferred to the mixing tank (G15) asshown on FIG. 14G. In embodiments, the large insect particulate portion(KCY) may be transferred to the multifunctional composition tank (6F1)on FIG. 14A, mixing tank (C15) on FIG. 14C, or to the interior (6A3)insect tank (6A2) of FIG. 14K. In embodiments, the third separator (KCR)separates a small insect particulate portion (KCW) from a large insectparticulate portion (KCY) using a screen (KM3) or a mesh (KM3′). Thescreen (KM3) or mesh (KM3′) have openings (KM4) that permit the smallinsect particulate portion (KCW) to pass through the openings (KM4). Theopenings (KM4) in the screen (KM3) or mesh (KM3′) are too small for thelarge insect particulate portion (KCY) to pass through.

In embodiments, the openings (KM4) in the screen (KM3) or mesh (KM3′)include Unites States Sieve size number 18, 20, 25, 30, 35, 40, 45, 50,60, 70, 80, 100, 120, 140, 170, 200, 230, 270, 325, or 400. Inembodiments, the openings (KM4) in the screen (KM3) or mesh (KM3′) havea size range that is selected from one or more from the group consistingof 37 microns to 44 microns, 44 microns to 53 microns, 53 microns to 63microns, 63 microns to 74 microns, 74 microns to 88 microns, 88 micronsto 105 microns, 105 microns to 125 microns, 125 microns to 149 microns,149 microns to 177 microns, 177 microns to 210 microns, 210 microns to250 microns, 250 microns to 297 microns, 297 microns to 354 microns, 354microns to 420 microns, 420 microns to 500 microns, 500 microns to 595microns, 595 microns to 707 microns, 707 microns to 841 microns, and 841microns to 1,000 microns.

In embodiments, the screen (KM3) or mesh (KM3′) may be cylindrical andlocated within a first chamber (KM5). In embodiments, the thirdseparator (KCR) has a third-first input (KCS) that is configured toreceive particulate insects that include first separated insects (KCG),second separated insects (KCP), and optionally additional separatedinsects (KDF). An auger (KM1) is configured to transfer the particulateinsects from the third-first input (KCS) to a screen (KM3) or mesh(KM3′) located within the first chamber (KM5) of the third separator(KCR). The auger (KM1) is equipped with a motor (KM2) that may beoperated by the computer (COMP). The particulate insects transferredfrom the third-first input (KCS) are sifted using a cylindrical screen(KM3) or mesh (KM3′) that is located within the first chamber (KM5).

The third-first output (KCT) is located at the bottom of the firstchamber (KM5). The small insect particulate portion (KCW) may be removedfrom the third separator (KCR) via the third-first output (KCT) locatedin the first chamber (KM5). The large insect particulate portion (KCY)that are too large to pass through openings (KM4) of the screen (KM3) ora mesh (KM3′) are transferred from the first chamber (KM5) to the secondchamber (KM6) of the third separator (KCR). Since the openings (KM4) inthe screen (KM3) or mesh (KM3′) within the first chamber (KM5) are toosmall for the large insect particulate portion (KCY) to pass through,the large insect particulate portion (KCY) is transferred from the firstchamber (KM5) to the second chamber (KM6) of the third separator (KCR).The large insect particulate portion (KCY) are removed from the secondchamber (KM6) of the third separator (KCR) via the third-second output(KCU).

In embodiments, the sifter is provided by the Kason Corporation. Inembodiments, sifter includes a vibratory screener or a centrifugalsifter. In embodiments, the sifter is provided by Kason Corporation andincludes a VIBRO SCREEN® Circular Vibratory Screener and Separator, aCENTRI-SIFTER™ High Capacity Screener and Separator, a VIBRO-BED™Circular Vibratory Fluid Bed Processor, or a CROSS-FLO High CapacityStatic Sieve Screener and Separator.

In embodiments, the motor (KM2) of the third separator (KCR) is drivenby a belt and ranges from 0.75 horsepower to 6 horsepower. Inembodiments, the motor (KM2) of the third separator (KCR) is driven by abelt and ranges from 0.56 kilowatts to 4.48 kilowatts. In embodiments,the motor (KM2) of the third separator (KCR) is not driven by a belt andranges from 0.5 horsepower to 4 horsepower. In embodiments, the motor(KM2) of the third separator (KCR) is driven by a belt and ranges from0.37 kilowatts to 2.98 kilowatts.

The fourth separator (KCZ) is connected to the condenser (KDH) via afourth transfer conduit (KDD). The third insect depleted gas stream(KDC) is transferred through the fourth transfer conduit (KDD) andenters the condenser (KDH). The third insect depleted gas stream (KDC)includes the vapor portion (KBV″) and gas portion (KBV′″) that weretransferred from the spray dryer (KAP).

The condenser (KDH) condenses the vapor portion (KBV″) which may includesteam. Liquid is formed from condensing the vapor portion (KBV″) of thethird insect depleted gas stream (KDC) to form process condensate (KDO).Liquid is formed from condensing steam contained within the third insectdepleted gas stream (KDC) to form process condensate (KDO). The processcondensate (KDO) is discharged from the condenser (KDH) via a liquidoutput (KDR).

The gas portion (KBV″) of the third insect depleted gas stream (KDC) isnot condensed within the condenser (KDH) and is instead released fromthe condenser (KDH) as a via the gas output (KDQ). The non-condensables(KDT) includes the gas portion (KBV′″) of the third insect depleted gasstream (KDC) and may include gas, air, nitrogen, carbon dioxide. Thenon-condensables (KDT) leave the gas output (KDQ) of the condenser (KDH)and are routed to a vacuum (KDM) via a gas transfer conduit (KDS).

In embodiments, the vacuum (KDM) is a vacuum pump, fan, or an eductor. Agas exhaust (KDN) is discharged from the vacuum (KDM). The gas exhaust(KDN) includes non-condensables (KDT) or the gas portion (KBV″) of thethird insect depleted gas stream (KDC) is not condensed within thecondenser (KDH).

The condenser (KDH) is provided with a cooling water input (KDI) and acooling water output (KDK). The cooling water input (KDI) is configuredto accept a cooling water supply (KDJ) and the cooling water output(KDK) is configured to discharge a cooling water return (KDL). Thecooling water supply (KDJ) is configured to condense a portion of thevapor that enters through the gas-vapor inlet (KDP).

Evaporator Operation: The systems shown in FIGS. 14G, 14H, and 14K,specifically, the biocatalyst mixing module (14G), exoskeletonseparation module (14H), and liquid separation module (LSM) can operatein a plurality of modes of operation, including:

(1) preparation of the insect liquid mixture (H39, KAS);

(2) start-up;

(3) normal operation;

(4) emergency shut-down;

(5) resuming operations after the emergency shut-down.

As seen in FIG. 14K, the liquid separation module (LSM) is equipped witha start-up/shut-down water system (KEZ). The purpose of thestart-up/shut-down water system (KEZ) is to make a pressurized andoptionally heated supply of water immediately available to theevaporator (KAO) whenever necessary. It is also desired to be able tomix a known flow of treated, filtered, start-up/shut-down water (KEO) inwith the insect liquid mixture (H39, KAS) to be used for start-up,shut-down or maintenance purposes such as cleaning.

A start-up/shut-down water tank (KEA) is provided and is configured toaccept a stream of water (KEB) from the output of the polishing unit(G41) shown in FIG. 14G. The water (KEB) transferred to the interior(KEA′) of the start-up/shut-down water tank (KEA) has passed through afilter (G23), activated carbon (G24), and/or an adsorbent (G25), firstwater treatment unit (G10), second water treatment unit (G11), thirdwater treatment unit (G12), and a cation (G39), an anion (G40), and apolishing unit (G41). The polishing unit (G41) may be any type ofconceivable device to improve the water quality such as an ultravioletunit, ozone unit, microwave unit, filter, a distillation system or thelike.

The start-up/shut-down water tank (KEA) may be equipped with a levelsensor (KES) that sends a signal (KET) to the computer (COMP). A levelcontrol valve (KEU) may be used to control the amount of water (KEB)that is transferred to the interior (KEA′) of the start-up/shut-downwater tank (KEA). The level control valve (KEU) may be equipped with acontroller (KEV) that is configured to input or output a signal (KEW) tothe computer (COMP). The computer (COMP), level control valve (KEU), andlevel sensor (KES) may be used together in a level control loop tomaintain a constant or batch supply of water to the interior (KEA′) ofthe start-up/shut-down water tank (KEA).

In embodiments, a start-up heat exchanger (KEP) is configured to heatthe water (KEB) that will be transferred to the evaporator (KAO). Inembodiments, a start-up heat exchanger (KEP) is configured to heat thewater (KEB) that will be transferred to the evaporator (KAO), spraydryer (KAP), rotary atomizer (KAU), spray nozzle (KBC) or plurality ofspray nozzles (KBC), or openings (KBC) or plurality of openings (KBC)within the disc (KBB) of the rotary atomizer (KAU). the purpose ofheating the water than will be transferred to the evaporator (KAO) isnot to provide a thermal shock on the system while can result in fouledheat transfer surfaces of the outer wall (KWG) within the interior(KBG′) of the drying chamber (KBG), and to prevent cloggage of eitherthe disc (KBB), spray nozzle (KBC), plurality of spray nozzles (KBC),opening (KBD), plurality of openings (KBD), spray aperture (KK4), ororifice (KK5).

Is it desired to heat the water (KEO, KEB) that is transferred to thespray dryer (KAP) so that a seamless transition from water (KEO, KEB) toan insect and liquid mixture (H39, KAS) can be realized to attainsteady-state conditions in the safest and most efficient manner aspossible.

In embodiments, it is necessary to be able to heat the water (KEB) priorto adding to the evaporator (KAO) by itself, or add the water (KEB) tothe evaporator (KAO) together while adding the insect liquid mixture(H39, KAS). Herein are disclosed methods to vary the flow of water (KEB)to an evaporator, such as a spray dryer, while varying either the flowof water (KEB) and/or the flow of insect liquid mixture (H39, KAS) tooptimize operations and efficiency while reducing plant maintenance andcleaning.

FIG. 14K shows the start-up heat exchanger (KEP) positioned within theinterior (KEA′) start-up/shut-down water tank (KEA). In embodiments, thestart-up heat exchanger (KEP) is located in between thestart-up/shut-down water tank (KEA) and the evaporator (KAO).

In embodiments, a water pump (KEK) is provided and configured totransfer water from the start-up/shut-down water tank (KEA) and into theevaporator (KAO). The water pump (KEK) is equipped with a motor (KEL)and a controller (KEM) which is configured to input or output a signal(KEN) to the computer (COMP).

In embodiments, a water control valve (KEF) is provided to control theflow of start-up/shut-down water (KEB, KEO) transferred from thestart-up/shut-down water tank (KEA) into the evaporator (KAO). The watercontrol valve (KEF) is equipped with a controller (KEG) that isconfigured to input or output a signal (KEH) to the computer (COMP).

In embodiments, a water flow sensor (KEI) is provided to measure theflow of start-up/shut-down water (KEB, KEO) transferred from thestart-up/shut-down water tank (KEA) into the evaporator (KAO). Inembodiments, the computer (COMP), water control valve (KEF), water flowsensor (KEI), are used in a flow control loop to control the amount ofwater (KEB, KEO) that is provided into the evaporator (KAO).

Herein is disclosed a method to start-up a spray dryer evaporator, themethod includes:

-   -   (a) providing:    -   (a0) providing an evaporator (KAO), spray dryer (KAP), rotary        atomizer (KAU), spray nozzle (KBC) or plurality of spray nozzles        (KBC), or openings (KBC) or plurality of openings (KBC) within a        disc (KBB) of the rotary atomizer (KAU);    -   (a1) an insect/liquid mixture valve (KEC) that is configured to        transfer a pressurized insect and liquid mixture (H39, KAS) to        the interior (KAP′) of the evaporator (KAO, KAP), the        insect/liquid mixture valve (KEC) is installed on an insect        liquid mixture conduit (H38);    -   (a2) a water valve (KEF) that is configured to transfer a        pressurized source of water (KEO, KEB) to the interior (KAP′) of        the evaporator (KAO, KAP), the water valve (KEF) is installed on        a water conduit (KEF′), the water (KEO, KEB) that is transferred        through the water conduit (KEF′) enters the liquid input (KAR)        of the evaporator (KAP, KAO) through a common portion (KAR′) of        the insect liquid mixture conduit (H38);    -   (b) transfer water (KEO, KEB) through the water valve (KEF) and        into the evaporator (KAO, KAP), while the insect/liquid mixture        valve (KEC) is closed;    -   (c) after step (b), open the insect/liquid mixture valve (KEC)        to and mix insect and liquid mixture (H39, KAS) with water in        the common portion (KAR′) of the insect liquid mixture conduit        (H38), wherein the flow of water (KEO, KEB) is greater than the        flow of insect liquid mixture (H39, KAS);

(d) after step (c), increase the flow of insect liquid mixture (H39,KAS) and decrease the flow of the water (KEO, KEB) so that the water(KEO, KEB) is equal to the flow of insect liquid mixture (H39, KAS) thatenters the evaporator (KAO);

(e) after step (d), increase the flow of insect liquid mixture (H39,KAS) and decrease the flow of the water (KEO, KEB) so that the water(KEO, KEB) is less than the flow of insect liquid mixture (H39, KAS)that enters the evaporator (KAO).

Herein is disclosed a method to start-up a spray dryer, the methodincludes:

-   -   (a) providing:    -   (a1) an insect/liquid mixture valve (KEC) that is configured to        transfer a pressurized insect and liquid mixture (H39, KAS) to a        spray dryer (KAP) through a rotary atomizer (KAU), spray nozzle        (KBC) or plurality of spray nozzles (KBC), or openings (KBC) or        plurality of openings (KBC) within a disc (KBB) of the rotary        atomizer (KAU), the insect/liquid mixture valve (KEC) is        installed on an insect liquid mixture conduit (H38);    -   (a2) a water valve (KEF) that is configured to transfer a        pressurized source of water (KEO, KEB) to a spray dryer (KAP)        through a rotary atomizer (KAU), spray nozzle (KBC) or plurality        of spray nozzles (KBC), the water valve (KEF) is installed on a        water conduit (KEF′), the water (KEO, KEB) that is transferred        through the water conduit (KEF′) enters the liquid input (KAR)        of the spray dryer (KAP) through a common portion (KAR′) of the        insect liquid mixture conduit (H38);    -   (b) transfer water (KEO, KEB) through the water valve (KEF) and        into the evaporator (KAO, KAP), while the insect/liquid mixture        valve (KEC) is closed;    -   (c) after step (b), open the insect/liquid mixture valve (KEC)        to and mix insect and liquid mixture (H39, KAS) with water in        the common portion (KAR′) of the insect liquid mixture conduit        (H38), wherein the flow of water (KEO, KEB) is greater than the        flow of insect liquid mixture (H39, KAS);    -   (d) after step (c), increase the flow of insect liquid mixture        (H39, KAS) and decrease the flow of the water (KEO, KEB) so that        the water (KEO, KEB) is equal to the flow of insect liquid        mixture (H39, KAS) that enters the evaporator (KAO);    -   (e) after step (d), increase the flow of insect liquid mixture        (H39, KAS) and decrease the flow of the water (KEO, KEB) so that        the water (KEO, KEB) is less than the flow of insect liquid        mixture (H39, KAS) that enters the evaporator (KAO).

Herein is disclosed a method to shut-down a spray dryer evaporator, themethod includes:

-   -   (a) providing:    -   (a0) providing an evaporator (KAO), spray dryer (KAP), rotary        atomizer (KAU), spray nozzle (KBC) or plurality of spray nozzles        (KBC), or openings (KBC) or plurality of openings (KBC) within a        disc (KBB) of the rotary atomizer (KAU);    -   (a1) an insect/liquid mixture valve (KEC) that is configured to        transfer a pressurized insect and liquid mixture (H39, KAS) to        the interior (KAP′) of the evaporator (KAO, KAP), the        insect/liquid mixture valve (KEC) is installed on an insect        liquid mixture conduit (H38);    -   (a2) a water valve (KEF) that is configured to transfer a        pressurized source of water (KEO, KEB) to the interior (KAP′) of        the evaporator (KAO, KAP), the water valve (KEF) is installed on        a water conduit (KEF′), the water (KEO, KEB) that is transferred        through the water conduit (KEF′) enters the liquid input (KAR)        of the evaporator (KAP, KAO) through a common portion (KAR′) of        the insect liquid mixture conduit (H38);    -   (b) transfer the insect and liquid mixture (H39, KAS) through        the insect/liquid mixture valve (KEC) and into the evaporator        (KAO, KAP), while the water valve (KEF) is closed;    -   (c) after step (b), open the water valve (KEF) and mix insect        and liquid mixture (H39, KAS) with water in the common portion        (KAR′) of the insect liquid mixture conduit (H38), wherein the        flow of water (KEO, KEB) is lesser than the flow of insect        liquid mixture (H39, KAS);    -   (d) after step (c), increase the flow of water (KEO, KEB) and        decrease the flow of the insect liquid mixture (H39, KAS) so        that the water (KEO, KEB) is equal to the flow of insect liquid        mixture (H39, KAS) that enters the evaporator (KAO);    -   (e) after step (d), increase the flow of water (KEO, KEB) and        decrease the flow of the insect liquid mixture (H39, KAS) so        that the water (KEO, KEB) is greater than the flow of insect        liquid mixture (H39, KAS) that enters the evaporator (KAO);    -   (f) after step (e), closing the insect/liquid mixture valve        (KEC) and stopping flow of the insect liquid mixture (H39, KAS)        into the evaporator (KAO).

Herein is disclosed a method to shut-down a spray dryer, the methodincludes:

-   -   (a) providing:    -   (a0) providing an evaporator (KAO), spray dryer (KAP), rotary        atomizer (KAU), spray nozzle (KBC) or plurality of spray nozzles        (KBC), or openings (KBC) or plurality of openings (KBC) within a        disc (KBB) of the rotary atomizer (KAU);    -   (a1) an insect/liquid mixture valve (KEC) that is configured to        transfer a pressurized insect and liquid mixture (H39, KAS) to a        spray dryer (KAP) through a rotary atomizer (KAU), spray nozzle        (KBC) or plurality of spray nozzles (KBC), or openings (KBC) or        plurality of openings (KBC) within a disc (KBB) of the rotary        atomizer (KAU), the insect/liquid mixture valve (KEC) is        installed on an insect liquid mixture conduit (H38);    -   (a2) a water valve (KEF) that is configured to transfer a        pressurized source of water (KEO, KEB) to a spray dryer (KAP)        through a rotary atomizer (KAU), spray nozzle (KBC) or plurality        of spray nozzles (KBC), or openings (KBC) or plurality of        openings (KBC) within a disc (KBB) of the rotary atomizer (KAU),        the water valve (KEF) is installed on a water conduit (KEF′),        the water (KEO, KEB) that is transferred through the water        conduit (KEF′) enters the liquid input (KAR) of the evaporator        (KAP, KAO) through a common portion (KAR′) of the insect liquid        mixture conduit (H38);    -   (b) transfer the insect and liquid mixture (H39, KAS) through        the insect/liquid mixture valve (KEC) and into the spray dryer        (KAP), while the water valve (KEF) is closed;    -   (c) after step (b), open the water valve (KEF) and mix insect        and liquid mixture (H39, KAS) with water in the common portion        (KAR′) of the insect liquid mixture conduit (H38), wherein the        flow of water (KEO, KEB) is lesser than the flow of insect        liquid mixture (H39, KAS);    -   (d) after step (c), increase the flow of water (KEO, KEB) and        decrease the flow of the insect liquid mixture (H39, KAS) so        that the water (KEO, KEB) is equal to the flow of insect liquid        mixture (H39, KAS) that enters the spray dryer (KAP);    -   (e) after step (d), increase the flow of water (KEO, KEB) and        decrease the flow of the insect liquid mixture (H39, KAS) so        that the water (KEO, KEB) is greater than the flow of insect        liquid mixture (H39, KAS) that enters the spray dryer (KAP);    -   (f) after step (e), closing the insect/liquid mixture valve        (KEC) and stopping flow of the insect liquid mixture (H39, KAS)        into the spray dryer (KAP).

In embodiments, a gas supply (KFD) is made available to the interior(KAP′) of the spray dryer (KAP). A gas supply valve (KFE) is madeavailable to regulate the amount of gas supply (KFD) that is introducedto the interior (KAP′) of the spray dryer (KAP). In embodiments, the gassupply (KFD) is made available to the interior (KAP′) of the spray dryer(KAP) for maintenance purposes to back-purge and unclog a spray nozzle(KBC), plurality of spray nozzles (KBC), opening (KBD), or plurality ofopenings (KBD). The gas supply (KFD) may include any gas, but preferablynitrogen, carbon dioxide, compressed air, a compressed oxygen-containinggas, etc. It is preferable that the gas supply (KFD) is pressurized. Inembodiments, the pressure of the gas supply may include any selectedfrom the group consisting of 5 pounds per square inch (PSI) to 10 PSI,10 PSI to 15 PSI, 15 PSI to 20 PSI, 20 PSI to 25 PSI, 25 PSI to 30 PSI,30 PSI to 35 PSI, 35 PSI to 40 PSI, 40 PSI to 45 PSI, 45 PSI to 50 PSI,50 PSI to 55 PSI, 55 PSI to 60 PSI, 60 PSI to 65 PSI, 65 PSI to 70 PSI,70 PSI to 75 PSI, 75 PSI to 80 PSI, 80 PSI to 85 PSI, 85 PSI to 90 PSI,90 PSI to 95 PSI, 95 PSI to 100 PSI, 100 PSI to 200 PSI, 200 PSI to 300PSI, 300 PSI to 400 PSI, 400 PSI to 500 PSI, 500 PSI to 1,000 PSI, 1,000PSI to 5,000 PSI, 5,000 PSI to 10,000 PSI, 10,000 PSI to 12,500 PSI,12,500 PSI to 13,500 PSI, and 13,500 PSI to 15,000 PSI

FIG. 14K shows a co-current spray dryer (KAP) evaporator (KAO). In FIG.14K the liquid input (KAR) is closer to the top (K-T) than the bottom(K-B). In FIG. 14K the gas input (KAQ) is closer to the top (K-T) thanthe bottom (K-B). In FIG. 14K the first output (KB S) is closer to thebottom (K-B) than the top (K-T). In FIG. 14K the second output (KBU) iscloser to the bottom (K-B) than the top (K-T). Here, the heated gassupply (KAG′) flows in the same direction of the insect liquid mixture(H39, KAS).

FIG. 14K-1:

FIG. 14K-1 shows one non-limiting embodiment of a co-current type ofspray dryer (KAP) that may be used with the liquid separation module(LSM) described in FIG. 14K.

Shown in FIGS. FIGS. 14K, 14K-1, 14K-2, 14K-3, and 14K-4, are differentembodiments of a spray dryer (KAP) having a top (K-T) bottom (K-B) thatare spaced apart along a vertical axis (KYY). The differences betweenthe different types of spray dryers shown in FIGS. 14K-1, 14K-2, 14K-3,and 14K-4 are the differences in height of various inputs and outputs,specifically, the differences in relative heights of: (A) the liquidinput (KAR) that introduces an insect liquid mixture (H39, KAS) to theinterior (KAP′) of the spray dryer (KAP); (B) the gas input (KAQ) thatintroduces a heated gas supply (KAG′) to the interior (KAP′) of thespray dryer (KAP); (C) first output (KBS) that discharges insects (KBT)from the from the interior (KAP′) of the spray dryer (KAP); and (D)second output (KBU) that evacuates an insect and gas mixture (KBV) awayfrom the interior (KAP′) of the spray dryer (KAP).

In FIG. 14K-1 the liquid input (KAR) is closer to the top (K-T) than thebottom (K-B). In FIG. 14K-1 the gas input (KAQ) is closer to the top(K-T) than the bottom (K-B). In FIG. 14K-1 the first output (KBS) iscloser to the bottom (K-B) than the top (K-T). In FIG. 14K-1 the secondoutput (KBU) is closer to the bottom (K-B) than the top (K-T). FIG.14K-1 shows a co-current spray dryer (KAP) evaporator (KAO) with theheated gas supply (KAG′) flowing in the same direction of the insectliquid mixture (H39, KAS).

FIG. 14K-2:

FIG. 14K-2 shows one non-limiting embodiment of a counter-current typeof spray dryer (KAP) that may be used with the liquid separation module(LSM) described in FIG. 14K.

In FIG. 14K-2 the liquid input (KAR) is closer to the top (K-T) than thebottom (K-B). In FIG. 14K-2 the gas input (KAQ) is closer to the bottom(K-B) than the top (K-T). In FIG. 14K-2 the first output (KBS) is closerto the bottom (K-B) than the top (K-T). In FIG. 14K-2 the second output(KBU) is closer to the top (K-T) than the bottom (K-B). FIG. 14K-2 showsa counter-current spray dryer (KAP) evaporator (KAO) with the heated gassupply (KAG′) flowing in a direction that is opposite to the flow of theinsect liquid mixture (H39, KAS). Here, the heated gas supply (KAG′)flows upwards from the gas input (KAQ) to the second output (KBU), whilethe insect liquid mixture (H39, KAS) is sprayed in a downwardsdirection.

FIG. 14K-3:

FIG. 14K-3 shows another non-limiting embodiment of a counter-currenttype of spray dryer (KAP) that may be used with the liquid separationmodule (LSM) described in FIG. 14K.

In FIG. 14K-3 the liquid input (KAR) is closer to the bottom (K-B) thanthe top (K-T). In FIG. 14K-3 the gas input (KAQ) is closer to the top(K-T) than the bottom (K-B). In FIG. 14K-3 the first output (KBS) iscloser to the bottom (K-B) than the top (K-T). In FIG. 14K-3 the secondoutput (KBU) is closer to the bottom (K-B) than the top (K-T).

FIG. 14K-3 shows a counter-current spray dryer (KAP) evaporator (KAO)with the heated gas supply (KAG′) flowing in a direction that isopposite to the flow of the insect liquid mixture (H39, KAS). Here, theheated gas supply (KAG′) flows downwards from the gas input (KAQ) to thesecond output (KBU), while the insect liquid mixture (H39, KAS) issprayed in an upwards direction.

FIG. 14K-4:

FIG. 14K-4 shows one non-limiting embodiment of a mixed-flow type ofspray dryer (KAP) that may be used with the liquid separation module(LSM) described in FIG. 14K.

In FIG. 14K-4 the liquid input (KAR) is closer to the bottom (K-B) thanthe top (K-T). In FIG. 14K-4 the gas input (KAQ) is closer to the top(K-T) than the bottom (K-B). In FIG. 14K-4 the first output (KBS) iscloser to the bottom (K-B) than the top (K-T). In FIG. 14K-4 the secondoutput (KBU) is second output (KBU) is closer to the bottom (K-B) thanthe top (K-T), the other (KBU′) is closer to the top (K-T) than thebottom (K-B).

FIG. 14K-4 shows a mixed-flow spray dryer (KAP) evaporator (KAO) withthe heated gas supply (KAG′) flowing in a direction that is opposite tothe flow of the insect liquid mixture (H39, KAS). Here, the heated gassupply (KAG′) flows both, in the same direction of the insect liquidmixture (H39, KAS), as well as opposite to the direction of the flow ofthe insect liquid mixture (H39, KAS). Here, the insect liquid mixture(H39, KAS) is sprayed in an upwards direction.

FIG. 14KK:

FIG. 14KK shows one non-limiting embodiment of aninsect-derived-biosensor including a transducer and aninsect-derived-biopolymer.

In embodiments, the biosensor is derived from the small insectparticulate portion (KCW) and/or the large insect particulate portion(KCY) that has undergone evaporation by spray drying as shown in FIG.14K. In embodiments, the biosensor is derived from the additionalseparated insects (KDF) that have undergone evaporation by spray dryingas shown in FIG. 14K.

The biosensor (14K1), includes: (a) a transducer (14K2); and (b) aninsect-derived-biopolymer (14K3); wherein: the insect-derived-biopolymerinteracts with a substance being tested and a biological response isconverted into an electrical signal by the transducer (14K2).

In embodiments, this disclosure describes a method to produce an insectbiopolymer:

(a) providing a source of insects;

(b) after step (a) mixing the insects with a caustic material and/or anoxidant and water to form an oxidized-insect-water mixture, the oxidantincludes hydrogen peroxide;

(c) after step (b), mixing the oxidized-insect-water mixture with abiocatalyst and optionally an acid to form an insect-liquid-mixture, thebiocatalyst includes one or more biocatalysts selected from the groupconsisting of an enzyme, casein protease, atreptogrisin A, flavorpro,peptidase, protease A, protease, Aspergillus oryzae, Bacillus subtilis,Bacillus licheniformis, Aspergillus niger, Aspergillus melleus,Aspergilus oryzae, papain, Carica papaya, bromelain, ananas comorusstem, a fungus, a microorganism, and yeast;

(d) after step (c), spray drying the insect-liquid-mixture to create aninsect and gas mixture; (e) after step (d), separating insects from theinsect and gas mixture wherein the insects include a powderedoligosaccharide;

(f) after step (e), producing a biosensor from the powderedoligosaccharide, the biosensor includes a transducer and theoligosaccharide;

wherein:

the oligosaccharide interacts with a substance being tested and abiological response is converted into an electrical signal by thetransducer.

In embodiments, the insect-derived-biopolymer is an oligosaccharidewhich interacts with a substance being tested and a biological responseis converted into an electrical signal by the transducer. Inembodiments, the oligosaccharide (G09′) may be used to produce abiosensor. In embodiments, the oligosaccharide (G09′) is aninsect-derived-biopolymer which may be used to produce the biosensor.

In embodiments, the oligosaccharide includes small insect particulateportion (KCW), the large insect particulate portion (KCY), or theadditional separated insects (KDF) that have undergone evaporation byspray drying as shown in FIG. 14K which may include a size range that isselected from one or more from the group consisting of 0.001 nanometersto 0.1 nanometers, 0.1 nanometers to 0.5 nanometers, 0.5 nanometers to 1nanometer, 1 nanometer to 5 nanometers, 5 nanometers to 10 nanometers,10 nanometers to 15 nanometers, 15 nanometers to 20 nanometers, 20nanometers to 25 nanometers, 25 nanometers to 30 nanometers, 30nanometers to 35 nanometers, 35 nanometers to 40 nanometers, 40nanometers to 45 nanometers, 45 nanometers to 50 nanometers, 50nanometers to 55 nanometers, 55 nanometers to 60 nanometers, 60nanometers to 65 nanometers, 65 nanometers to 70 nanometers, 70nanometers to 75 nanometers, 75 nanometers to 80 nanometers, 80nanometers to 85 nanometers, 85 nanometers to 90 nanometers, 90nanometers to 95 nanometers, 95 nanometers to 100 nanometers, 100nanometers to 200 nanometers, 200 nanometers to 300 nanometers, 300nanometers to 400 nanometers, 400 nanometers to 500 nanometers, 500nanometers to 600 nanometers, 600 nanometers to 700 nanometers, 700nanometers to 800 nanometers, and 800 nanometers to 900 nanometers.

In embodiments, the biosensor (14K1) may be used for biosensorapplications including environmental, agricultural, medicinal, and foodindustrial market sectors. In embodiments, the insect-derived-biopolymer(14K3) is an oligosaccharide. In embodiments, theinsect-derived-biopolymer (14K3) is applied to the biosensor via screenprinting, drop coating, and/or deposited using enzymes onto the surfaceof the sensor. In embodiments, the present disclosure provides foroligosaccharide printed biosensors (14K1). In embodiments, the biosensor(14K1) is an electrochemical biosensor (14K1) including aninsect-derived-biopolymer (14K3). In embodiments, the biosensor (14K1)can be a tool to use for detecting pathogens, molecular diagnostics,monitoring the environment, and controlling food safety and defendingthe homeland of the United States of America.

Herein is disclosed an insect-derived electrochemical biosensor that isnot expensive, easy to use, and extremely small-scale and miniature. Inembodiments, the biosensor (14K1) can detect ammonia, pyruvate,cholesterol, lactase, glucose, can detect if a human is pregnant, candetect if a mammal is pregnant, can detect if a reptile is pregnant, candetect if an insect is pregnant, can detect if an amphibian is pregnant.In embodiments, the biosensor (14K1) transduces a process ofbio-recognition into signals that can be understood via the transducer(14K2) and the insect-derived-biopolymer (14K3). In embodiments, thebiosensor (14K1) can be used in clinical diagnostics due to its highsensitivity and selectivity. In embodiments, the biosensor (14K1) can beused in hospitals, urgent-care centers, or remotely-located physicians,or veterinarian centers to perform a wide variety of medical tests on apatient.

In embodiments, the biosensor (14K1) can be used to diagnose diseasessuch as diabetes, cardiovascular disease, optical corrections,regenerative medicine, cancer, and for therapeutic applications. Inembodiments, the biosensor (14K1) can detect cancer in humans and inmammals. In embodiments, the insect-derived-biopolymer (14K3) portion ofthe biosensor (14K1) captures analytes. In embodiments, the transducer(14K2) portion of the biosensor (14K1) converts a binding event of theinsect-derived-biopolymer (14K3) to a measurable signal variation. Inembodiments, the biosensor (14K1) can recognize biomolecules includingone or more biomolecules selected from the group consisting ofantibodies, immunosensors, protein receptors, enzymes, whole cells, andnucleic acids. In embodiments, the biosensor (14K1) can be used for drugdelivery, disease detection, prosthetic devices, environmentalmonitoring, water quality management, monitoring soil quality, measuringtoxins in defense or military combat applications, and monitoring foodquality.

In embodiments, the biosensor (14K1) has a potential including one ormore potentials selected from the group consisting of −60 millivolts to−55 millivolts, −55 millivolts to −50 millivolts, −50 millivolts to −45millivolts, −45 millivolts to −40 millivolts, −40 millivolts to −35millivolts, −35 millivolts to −30 millivolts, −30 millivolts to −25millivolts, −25 millivolts to −20 millivolts, −20 millivolts to −15millivolts, −15 millivolts to −10 millivolts, −10 millivolts to −5millivolts, −5 millivolts to 0 millivolts, 0 millivolts to 5 millivolts,5 millivolts to 10 millivolts, 10 millivolts to 15 millivolts, 15millivolts to 20 millivolts, 20 millivolts to 25 millivolts, 25millivolts to 30 millivolts, 30 millivolts to 35 millivolts, 35millivolts to 40 millivolts, 40 millivolts to 45 millivolts, 45millivolts to 50 millivolts, 50 millivolts to 55 millivolts, 55millivolts to 60 millivolts, 60 millivolts to 65 millivolts, 65millivolts to 70 millivolts, and 70 millivolts to 75 millivolts.

In embodiments, the biosensor (14K1) has a voltammetry having aconduction including one or more selected from the group consisting of1.000 e²/h to 1.250 e²/h, 1.250 e e²/h to 1.500 e²/h 1.500 e²/h to 1.750e²/h, 1.750 e²/h to 2.000 e²/h, 2.000 e²/h to 2.250 e²/h, 2.250 e²/h to2.500 e²/h, 2.500 e²/h to 2.750 e²/h, 2.750 e²/h to 3.000 e²/h, 3.000e²/h to 3.250 e²/h, 3.250 e²/h to 3.500 e²/h, 3.500 e²/h to 3.750 e²/h,3.750 e²/h to 4.000 e²/h, 4.000 e²/h to 4.250 e²/h, 4.250 e²/h to 4.500e²/h, 4.500 e²/h to 4.750 e²/h, 4.750 e²/h to 5.000 e²/h, 5.000 e²/h to5.250 e²/h, 5.250 e²/h to 5.500 e²/h, 5.500 e²/h to 5.750 e²/h, 5.750e²/h to 6.000 e²/h, 6.000 e²/h to 6.250 e²/h, 6.250 e²/h to 6.500 e²/h,6.500 e²/h to 6.750 e²/h, 6.750 e²/h to 7.000 e²/h, 7.000 e²/h to 7.250e²/h, 7.250 e²/h to 7.500 e²/h, 7.500 e²/h to 7.750 e²/h, 7.750 e²/h to8.000 e²/h, and 8.000 e e²/h to 8.250 e²/h. This units e²/h measure theconductance quantum of the biosensor (14K1).

In embodiments, the biosensor (14K1) has an amperometry including one ormore selected from the group consisting of −0.000050 amps to −0.000045amps, −0.000045 amps to −0.000040 amps, −0.000040 amps to −0.000035amps, −0.000035 amps to −0.000030 amps, −0.000030 amps to −0.000025amps, −0.000025 amps to −0.000020 amps, −0.000020 amps to −0.000015amps, −0.000015 amps to −0.000010 amps, −0.000010 amps to −0.000005amps, −0.000005 amps to 0.000000 amps, 0.000000 amps to 0.000005 amps,0.000005 amps to 0.000010 amps, 0.000010 amps to 0.000015 amps, 0.000015amps to 0.000020 amps, 0.000020 amps to 0.000025 amps, 0.000025 amps to0.000030 amps, 0.000030 amps to 0.000035 amps, 0.000035 amps to 0.000040amps, 0.000040 amps to 0.000045 amps, 0.000045 amps to 0.000050 amps,and 0.000050 amps to 0.000055 amps.

In embodiments, the biosensor (14K1) has a conductance including one ormore selected from the group consisting of 0.01 microsiemens to 0.02microsiemens, 0.02 microsiemens to 0.04 microsiemens, 0.04 microsiemensto 0.08 microsiemens, 0.08 microsiemens to 0.10 microsiemens, 0.10microsiemens to 0.50 microsiemens, 0.50 microsiemens to 0.75microsiemens, 0.75 microsiemens to 1.00 microsiemens, 1.00 microsiemensto 1.25 microsiemens, 1.25 microsiemens to 1.50 microsiemens, 1.50microsiemens to 1.75 microsiemens, 1.75 microsiemens to 2.00microsiemens, 2.00 microsiemens to 2.50 microsiemens, 2.50 microsiemensto 3.00 microsiemens, 3.00 microsiemens to 3.50 microsiemens, 3.50microsiemens to 4.00 microsiemens, 4.00 microsiemens to 4.50microsiemens, 4.50 microsiemens to 5.00 microsiemens, 5.00 microsiemensto 5.50 microsiemens, 5.50 microsiemens to 6.00 microsiemens, 6.00microsiemens to 6.50 microsiemens, 6.50 microsiemens to 7.00microsiemens, 7.00 microsiemens to 7.50 microsiemens, 7.50 microsiemensto 8.00 microsiemens, 8.00 microsiemens to 8.50 microsiemens, 8.50microsiemens to 9.00 microsiemens, 9.00 microsiemens to 9.50microsiemens, and 9.50 microsiemens to 10.00 microsiemens.

FIG. 14L:

FIG. 14L shows a power production system (PPS) that is configured togenerate electricity, heat, or steam for use in the Insect ProductionSuperstructure System (IPSS).

In embodiments, the power production system (PPS) shown in FIG. 14L cangenerate electricity for use in the Insect Production SuperstructureSystem (IPSS). In embodiments, the power production system (PPS) shownin FIG. 14L can generate steam for use in the Insect ProductionSuperstructure System (IPSS). In embodiments, the power productionsystem (PPS) shown in FIG. 14L can generate heat for use in the InsectProduction Superstructure System (IPSS). In embodiments, the powerproduction system (PPS) includes a compressor (LEB), a combustor (LED),a turbine (LFE), a generator (LFH), a HRSG (heat recovery steamgenerator) (LFI), a steam drum (LBE), a steam distribution header (LCJ),and a condensate tank (LAP).

An oxygen-containing gas (LEA) is made available to a compressor (LEB).In embodiments, the oxygen-containing gas may be air,oxygen-enriched-air i.e. greater than 21 mole % O2, and substantiallypure oxygen, i.e. greater than about 95 mole % oxygen (the remainderusually comprising N2 and rare gases). In embodiments, theoxygen-containing gas may be flue gas or carbon dioxide. In embodiments,flue gas includes a vapor or gaseous mixture containing varying amountsof nitrogen (N2), carbon dioxide (CO2), water (H2O), and oxygen (O2). Inembodiments, flue gas is generated from the thermochemical process ofcombustion. In embodiments, combustion is an exothermic (releases heat)thermochemical process wherein at least the stoichiometric oxidation ofa carbonaceous material takes place to generate flue gas.

In embodiments, the compressor (LEB) has a plurality of stages (LEC). Inembodiments, the compressor (LEB) is an axial compressor. Inembodiments, the compressor is configured to compress and pressurize theoxygen-containing gas (LEA) to form a compressed gas stream (LEK). Inembodiments, the compressor is configured to compress and pressurize theoxygen-containing gas (LEA) to form a first compressed gas stream (LEK)and a second compressed gas stream (LEN). In embodiments, compressed gasstream (LEK) is provided to a combustor (LED). In embodiments, the firstcompressed gas stream (LEK) is provided to a first combustor (LED1). Inembodiments, the second compressed gas stream (LEN) is provided to asecond combustor (LED2).

In embodiments, the first combustor (LED1) has a first gas mixer (LEE).In embodiments, the second combustor (LED2) has a second gas mixer(LEH). In embodiments, the first gas mixer (LEE) or second gas mixer(LEH) is that of an annular type. In embodiments, the first combustor(LED1) or second combustor (LED2) is that of an annular type. Inembodiments, the annular type gas mixer (LEE) mixes the fuel with theoxygen containing-gas within the combustor to form afuel-and-oxygen-containing gas mixture, which is then combusted. Inembodiments, the first combustor (LED1) has a first ignitor (LEF). Inembodiments, the second combustor (LED2) has a second ignitor (LEI). Inembodiments, the first ignitor (LEF) or second ignitor (LEI) include atorch ignitor. In embodiments, the first ignitor (LEF) or second ignitor(LEI) include a separate fuel supply to maintain a constantly burningtorch. In embodiments, the first combustor (LED1) has a first flamedetector (LEG). In embodiments, the second combustor (LED2) has a secondflame detector (LEJ). In embodiments, the first flame detector (LEG) orsecond flame detector (LEJ) are selected from one or more from the groupconsisting of a UV flame detector, IR flame detector, UV/IR flamedetector, multi-spectrum infrared flame detector, and a visual flameimaging flame detector.

In embodiments, the combustor (LED) mixes and combusts the compressedgas stream (LEK) with a first fuel (LEL) to produce a combustion stream(LEM). In embodiments, the first combustor (LED1) mixes and combusts thefirst compressed gas stream (LEK) with a first fuel (LEL) to produce afirst combustion stream (LEM). In embodiments, the first combustionstream (LEM) is a first pressurized combustion stream (LEM′). Inembodiments, the second combustor (LED2) mixes and combusts the secondcompressed gas stream (LEN) with a second fuel (LEO) to produce a secondcombustion stream (LEP). In embodiments, the second combustion stream(LEP) is a second pressurized combustion stream (LEP′).

A first fuel valve (LEW) is provided to regulate the flow of thecompressor fuel source (LEU) to the first combustor (LED1) and thesecond combustor (LED2). The first fuel valve (LEW) is equipped with acontroller (LEX) that is configured to input or output a signal (LEY) tothe computer (COMP). FIG. 14L shows connector (K1) to show continuitybetween the second fuel (LEO) that is apportioned from the compressorfuel source (LEU) and transferred to the second combustor (LED2).

The combustion stream (LEM) is transferred to a turbine (LFE). Inembodiments, the first combustion stream (LEM) is combined with thesecond combustion stream (LEP) before being transferred to the turbine(LFE). In embodiments, the turbine (LFE) has a plurality of stages(LFF). In embodiments, the first and second combustion streams (LEM,LEP) rotate a portion of the turbine (LFE), which in turn rotates ashaft (LFG), and a generator (LFH) to produce electricity (ELEC). Inembodiments, the combustion stream (LEM) rotates the turbine (LFE),which in turn rotates a shaft (LFG), and a generator (LFH) to produceelectricity (ELEC).

In embodiments, the compressor (LEB) is connected to the turbine (LFE)via a shaft (LFG). In embodiments, the turbine (LFE) is connected to thegenerator (LFH) via a shaft (LFG). In embodiments, the turbine (LFE)rotates the shaft (LFG) which in turn drives the compressor (LEB). Inembodiments, the generator (LFH) is connected to the turbine (LFE) via ashaft (LFG). In embodiments, the turbine (LFE) rotates the shaft (LFG)which in turn drives the generator (LFH) to produce electricity for usein the Insect Production Superstructure System (IPSS).

FIG. 14L shows the generator (LFH) producing electricity for use in thecomputer (COMP) within the Insect Production Superstructure System(IPSS). FIG. 14L shows the generator (LFH) producing electricity for usein the computer (COMP) within the farming superstructure system (FSS).In embodiments, the electricity (ELEC) may be used in the InsectProduction Superstructure System (IPSS) in any number of a plurality of:sensors, motors, pumps, heat exchangers, fans, actuators, controllers,compressors, analyzers, computers, lights, heaters, vacuum pumps, etc.Any asset, including sensors, motors, pumps, heat exchangers, fans,actuators, controllers, compressors, analyzers, computers, lights,heaters, vacuum pumps, disclosed in FIGS. 1A through 48 may be poweredby the electricity (ELEC) generated by the generator (LFH) or generator(LCA).

A combustion stream (LFD) is discharged from the turbine (LFE) and isrouted to a HRSG (LFI). In embodiments, the combustion stream (LFD) thatis discharged from the turbine (LFE) is a depressurized combustionstream (LFD′). In embodiments the depressurized combustion stream (LFD′)has a pressure that is less than the pressure of the combustion stream(LEM, LEP) that is transferred to the turbine (LFE). The combustionstream (LFD) is transferred from the turbine (LFE) to the HRSG (LFI).The HRSG (LFI) is configured to remove heat from the combustion stream(LFD) by use of a heat transfer conduit (LBI) or a plurality of heattransfer conduits (LBI). At least one heat transfer conduit (LBI)generates steam through indirect heat transfer from the combustionstream (LFD).

In embodiments, the HRSG (LFI) is a fired-HRSG (LFJ). In embodiments,the fired-HRSG (LFJ) accepts a HRSG fuel source (LEV). In embodiments,the HRSG fuel source (LEV) is combusted with the combustion stream (LFD)that is transferred from the turbine (LFE) to form a combustion stream(LX0′). In embodiments, the HRSG fuel source (LEV) is combusted with anoxygen-containing gas (LX0). In the instance where the HRSG fuel source(LEV) is combusted with an oxygen-containing gas (LX0), the compressor(LEB), a combustor (LED), a turbine (LFE), a generator (LFH) areoptional. Thus, saturated steam (LBR) or superheated steam (LB S) may begenerated within the steam drum (LBE) by combusting an oxygen-containinggas (LX0) with the compressor fuel source (LEU) to form a combustionstream (LX0′).

In embodiments, a second fuel valve (LFA) is made available to regulatethe amount of the HRSG fuel source (LEV) that is introduced to thefired-HRSG (LFJ). The second fuel valve (LFA) is equipped with acontroller (LFB) that is configured to input or output a signal (LFC) tothe computer (COMP). In embodiments, the compressor fuel source (LEU)and HRSG fuel source (LEV) come from a common fuel source (LEQ). Acompressor fuel source (LEU) provides the fuel that is used as the firstfuel (LEL) and second fuel (LEO). In embodiments, the fuel source (LEQ)that is made available as the compressor fuel source (LEU) or HRSG fuelsource (LEV) may include a hydrocarbon. In embodiments, the fuel source(LEQ) that is made available as the compressor fuel source (LEU) or HRSGfuel source (LEV) may be a liquid, vapor, or a gas. In embodiments, thefuel source (LEQ) that is made available as the compressor fuel source(LEU) or HRSG fuel source (LEV) may be a methane containing gas such asnatural gas. In embodiments, the fuel source (LEQ) that is madeavailable as the compressor fuel source (LEU) or HRSG fuel source (LEV)may be naphtha, natural gas, gasoline, a hydrocarbon, diesel, or oil. Inembodiments, the fuel source (LEQ, LET, LEU, LEV), may include ahydrocarbon, and may be a liquid, vapor, or a gas. In embodiments, thefuel source (LEQ, LET, LEU, LEV), may be a methane containing gas suchas natural gas, or otherwise may be naphtha, natural gas, gasoline, ahydrocarbon, diesel, or oil.

In embodiments, a fuel source (LEQ) is made available to a fuelcompressor (LER) to form a compressed fuel (LET). In embodiments, thefuel compressor (LER) has a plurality of stages (LES). A pressure sensor(LEQP) is provided to measure the pressure of the fuel source (LEQ) thatis made available to the fuel compressor (LER). In embodiments, thecompressor fuel source (LEU) and HRSG fuel source (LEV) are a compressedfuel (LET). In embodiments, the HRSG fuel source (LEV) is combustedwithin the fired-HRSG (LFJ) using a burner (LFK) such as a duct burner.In embodiments, the fired-HRSG (LFJ) or the burner (LFK) is lined withrefractory material. In embodiments, the refractory material includes aceramic, alumina, silica, magnesia, silicon carbide, or graphite.

In embodiments, heat is removed from the HRSG (LFI) and a flue gas (LFP)is evacuated from the HRSG (LFI). In embodiments, heat is removed fromthe fired-HRSG (LFJ) and a flue gas (LFP) is evacuated from thefired-HRSG (LFJ). A temperature sensor (LFM) is configured to measurethe temperature within the HRSG (LFI, LFJ). A temperature sensor (LFM)is configured to measure the temperature of the flue gas (LFP) that isdischarged from the HRSG (LFI, LFJ).

In embodiments, at least a portion of the flue gas (LFP) is madeavailable as flue gas (FG1) that may be transferred to the thermalcompressor (Q30) on FIG. FIG. 27D or 27F. In embodiments, at least aportion of the flue gas (LFP) is made available as flue gas (FG1) thatmay be transferred to the generator (Q50) within the thermal compressor(Q30) on FIG. 27D or 27F.

The steam generated in the plurality of heat transfer conduits (LBI) isrouted to a steam drum (LBE). In embodiments, the steam drum (LBE)generates saturated steam (LBR) or superheated steam (LBS). Inembodiments, saturated steam (LBR) is discharged from the steam drum(LBE) and is routed to a superheater (LX3) through a saturated steamtransfer conduit (LX1). Heat is transferred from the combustion stream(LFD, LX0′) to saturated steam (LBR) within the superheater (LX3) toproduce superheated steam (LBS) which is routed to a superheated steamtransfer conduit (LX2).

A steam distribution header (LCJ) is configured to accept at least aportion of the saturated steam (LBR) or superheated steam (LBS). Inembodiments, a first portion (LBW) of either the saturated steam (LBR)or superheated steam (LBS) is transferred through a first steam transferconduit (LBY) and into the steam distribution header (LCJ). Inembodiments, a second portion (LBX) of either the saturated steam (LBR)or superheated steam (LBS) is transferred through a second steamtransfer conduit (LSY) and into steam turbine (LBZ) to generateelectricity via a generator (LCA). In embodiments, the steam turbine(LBZ) has a plurality of stages (LBZX). The steam turbine (LBZ) isconnected to a generator (LCA) via a shaft (LCB). Depressurized steam(LCI) is evacuated from the steam turbine (LBZ) and is routed towardsthe steam distribution header (LCJ).

FIG. 14L shows a steam distribution header (LCJ) that is configured toaccept at least a portion of the saturated steam (LBR) or superheatedsteam (LBS) that are routed through either the first steam transferconduit (LBY) or second steam transfer conduit (LSY). A pressure sensor(LBO) is provided to measure the pressure within the interior of thesteam drum (LBE). A temperature sensor (LBQ) is provided to measure thetemperature of the saturated steam (LBR) or superheated steam (LBS) thatare discharged from the steam drum (LBE). A pressure control valve (LBT)is positioned on the steam distribution header (LCJ). In embodiments,the pressure control valve (LBT) controls the pressure within the steamdrum (LBE). In embodiments, the pressure control valve (LBT) controlsthe pressure within first steam transfer conduit (LBY) and second steamtransfer conduit (LSY). The pressure control valve (LBT) is equippedwith a controller (LBU) that sends a signal (LBV) to or from thecomputer (COMP). In embodiments, the computer (COMP), pressure controlvalve (LBT), and pressure sensor (LBO) are used in a control loop toregulate the pressure within the steam drum (LBE), first steam transferconduit (LBY), or second steam transfer conduit (LSY).

In embodiments, the steam distribution header (LCJ) provides a source ofsteam to a variety of locations within the Insect ProductionSuperstructure System (IPSS). In embodiments, the velocity of steamwithin the steam distribution header (LCJ) ranges from one or more fromthe group selected from 50 feet per second (FPS) to 60 FPS, 60 FPS to 70FPS, 70 FPS to 80 FPS, 80 FPS to 90 FPS, 90 FPS to 100 FPS, 100 FPS to110 FPS, 110 FPS to 120 FPS, 120 FPS to 130 FPS, 130 FPS to 140 FPS, 140FPS to 150 FPS, 150 FPS to 160 FPS, 160 FPS to 180 FPS, 180 FPS to 200FPS, 200 FPS to 225 FPS, and 225 FPS to 250 FPS.

In embodiments, the steam distribution header (LCJ) operates at apressure range that is selected from one or more from the groupconsisting of 5 pounds per square inch (PSI) 10 PSI, 10 PSI 20 PSI, 20PSI 30 PSI, 30 PSI 40 PSI, 40 PSI 50 PSI, 50 PSI 60 PSI, 60 PSI 70 PSI,70 PSI 80 PSI, 80 PSI 90 PSI, 90 PSI 100 PSI, 100 PSI 125 PSI, 125 PSI150 PSI, 150 PSI 175 PSI, 175 PSI 200 PSI, 200 PSI 225 PSI, 225 PSI 250PSI, 250 PSI 275 PSI, 275 PSI 300 PSI, 300 PSI 325 PSI, 325 PSI 350 PSI,350 PSI 375 PSI, 375 PSI 400 PSI, 400 PSI 425 PSI, 425 PSI 450 PSI, 450PSI 475 PSI, 475 PSI 500 PSI, 500 PSI 525 PSI, 525 PSI 550 PSI, 550 PSI575 PSI, 575 PSI 600 PSI, 600 PSI 700 PSI, 700 PSI 800 PSI, 800 PSI 900PSI, and 900 PSI 1,000 PSI.

In embodiments, the steam distribution header (LCJ) is insulated withinsulation (LCJ′). In embodiments, the range of thickness of theinsulation (LCJ′) on the steam distribution header (LCJ) is selectedfrom one or more from the group consisting of 1 inches to 1.5 inches,1.5 inches to 2 inches, 2 inches to 2.5 inches, 2.5 inches to 3 inches,3 inches to 3.5 inches, 3.5 inches to 4 inches, 4 inches to 4.5 inches,4.5 inches to 5 inches, 5 inches to 5.5 inches, 5.5 inches to 6 inches,6 inches to 6.5 inches, 6.5 inches to 7 inches, 7 inches to 7.5 inches,7.5 inches to 8 inches, 8 inches to 8.5 inches, 8.5 inches to 9 inches,9 inches to 9.5 inches, 9.5 inches to 10 inches, 10 inches to 11 inches,11 inches to 12 inches, 12 inches to 13 inches, 13 inches to 14 inches,14 inches to 15 inches, 15 inches to 16 inches, 16 inches to 17 inches,and 17 inches to 18 inches.

In embodiments, the steam distribution header (LCJ) provides a source ofsteam to a variety of locations including: a first steam supply (LCL) toFIG. 3, Feeding Chamber (FC1, FC2, FC3), air heater (264); a secondsteam supply (LCP) to FIG. 13, heat exchanger (HX1580); a third steamsupply (LCT) to FIG. 14C, heat exchanger (C53); a fourth steam supply(LCX) to FIG. 14E, heat exchanger (E20); a fifth steam supply (LDB) toFIG. 14G, heating jacket (G53J) and/or to the heat exchanger (G53); asixth steam supply (LDF) to FIG. 14H, heat exchanger (H34); a seventhsteam supply (LDJ) to FIG. 14J, evaporator (J11) heating jacket (J17);an eighth steam supply (LDM) to FIG. 14K, air heater (KAF); a ninthsteam supply (LDP) to FIG. 14K, drying chamber (KBG) heating jacket(KBJ); a tenth steam supply (LDS) to FIG. 27D, thermal compressor (Q30);an eleventh steam supply (LDV) to FIG. 34B, thermal compressor (QQ30).

In embodiments, a first steam valve (LCM) is configured to regulate theamount of the first steam supply (LCL) to FIG. 3, Feeding Chamber (FC1),air heater (264). A first reducer (LCN) may be positioned upstream ordownstream of the first steam valve (LCM) on the steam distributionheader (LCJ).

In embodiments, a second steam valve (LCQ) is configured to regulate theamount of the second steam supply (LCP) to FIG. 13, heat exchanger(HX1580). A second reducer (LCR) may be positioned upstream ordownstream of the second steam valve (LCQ) on the steam distributionheader (LCJ).

In embodiments, a third steam valve (LCU) is configured to regulate theamount of the third steam supply (LCT) to FIG. 14C, heat exchanger(C53). A third reducer (LCV) may be positioned upstream or downstream ofthe third steam valve (LCU) on the steam distribution header (LCJ).

In embodiments, a fourth steam valve (LCY) is configured to regulate theamount of the fourth steam supply (LCX) to FIG. 14E, heat exchanger(E20). A fourth reducer (LCZ) may be positioned upstream or downstreamof the fourth steam valve (LCY) on the steam distribution header (LCJ).

In embodiments, a fifth steam valve (LDC) is configured to regulate theamount of the fifth steam supply (LDB) to FIG. 14G, heating jacket(G53J) and/or to the heat exchanger (G53). A fifth reducer (LDD) may bepositioned upstream or downstream of the fifth steam valve (LDC) on thesteam distribution header (LCJ).

In embodiments, a sixth steam valve (LDG) is configured to regulate theamount of the sixth steam supply (LDF) to FIG. 14H, heat exchanger(H34). A sixth reducer (LDH) may be positioned upstream or downstream ofthe sixth steam valve (LDG) on the steam distribution header (LCJ).

In embodiments, a seventh steam valve (LDK) is configured to regulatethe amount of the seventh steam supply (LDJ) to FIG. 14J, evaporator(J11) heating jacket (J17). A seventh reducer (LDL) may be positionedupstream or downstream of the seventh steam valve (LDK) on the steamdistribution header (LCJ).

In embodiments, an eighth steam valve (LDN) is configured to regulatethe amount of the eighth steam supply (LDM) to FIG. 14K, air heater(KAF). An eighth reducer (LDO) may be positioned upstream or downstreamof the eighth steam valve (LDN) on the steam distribution header (LCJ).

In embodiments, a ninth steam valve (LDQ) is configured to regulate theamount of the ninth steam supply (LDP) to FIG. 14K, drying chamber (KBG)heating jacket (KBJ). A ninth reducer (LDR) may be positioned upstreamor downstream of the ninth steam valve (LDQ) on the steam distributionheader (LCJ).

In embodiments, a tenth steam valve (LDT) is configured to regulate theamount of the tenth steam supply (LDS) to FIG. 27D, thermal compressor(Q30) A tenth reducer (LDU) may be positioned upstream or downstream ofthe tenth steam valve (LDT) on the steam distribution header (LCJ).

In embodiments, an eleventh steam valve (LDW) is configured to regulatethe amount of the eleventh steam supply (LDV) to FIG. 34B, thermalcompressor (QQ30) An eleventh reducer (LDX) may be positioned upstreamor downstream of the eleventh steam valve (LDW) on the steamdistribution header (LCJ).

In embodiments, a twelfth steam valve (LZB) is configured to regulatethe amount of the twelfth steam supply (LZC) to FIG. 12C, hydrogenationsystem (2C13). An twelfth reducer (LZA) may be positioned upstream ordownstream of the twelfth steam valve (LZB) on the steam distributionheader (LCJ). In turn, a plurality of steam condensate streams aretransferred from various locations within the IPSS and are returned to acondensate tank (LAP) as indicated on FIG. 14L. In embodiments, thecondensate tank (LAP) accepts steam condensate streams are transferredfrom various locations, including: a first condensate (LAQ) from FIG. 3,Feeding Chamber (FC1, FC2, FC3), air heater (264); a second condensate(LAR) from FIG. 13, heat exchanger (HX1580); a third condensate (LAS)from FIG. 14C, heat exchanger (C53); a fourth condensate (LAT) from FIG.14E, heat exchanger (E20); a fifth condensate (LAU) from FIG. 14G,heating jacket (G53J) and/or to the heat exchanger (G53); a sixthcondensate (LAV) from FIG. 14H, heat exchanger (H34); a seventhcondensate (LAW) from FIG. 14J, evaporator (J11) heating jacket (J17);an eighth condensate (LJA) from FIG. 14K, air heater (KAF); a ninthcondensate (LJB) from FIG. 14K, drying chamber (KBG) heating jacket(KBJ); a tenth condensate (LJC) from FIG. 27D, thermal compressor (Q30);an eleventh condensate (LJD) from FIG. 34B, thermal compressor (QQ30).

In embodiments, at least a portion are used again to remove heat withinthe HRSG (LFI, LFJ): first condensate (LAQ), second condensate (LAR),third condensate (LAS), fourth condensate (LAT), fifth condensate (LAU),sixth condensate (LAV), seventh condensate (LAW), eighth condensate(LJA), ninth condensate (LJB), tenth condensate (LJC), eleventhcondensate (LJD). In embodiments, feed water (LAX) (which may includecondensate (LAQ, LAR, LAW, LAT, LAU, LAV, LAW, LJA, LJB, LJC, LJD)) ispumped to the from the condensate tank (LAP) to the steam drum input(LBD) of the steam drum (LBE) via a pump (LAX′).

A heat exchanger (LAZ) is provided to pre-heat the feed water (LAX) asit is transferred from the condensate tank (LAP) to the steam drum(LBE). A temperature sensor (LAY) is provided to measure the temperatureof the feed water (LAX) before it enters the heat exchanger (LAZ).Another temperature sensor (LBC) is provided to measure the temperatureof the feed water (LAX) after is exits the heat exchanger (LAZ).

In embodiments, the steam drum (LBE) is equipped with a level sensor(LBP) that is configured to regulate the amount of feed water (LAX) thatis introduced to the steam drum (LBE). In embodiments, the steam drum(LBE) is equipped with a level control valve (LBP′) that is configuredto regulate the amount of feed water (LAX) that is introduced to thesteam drum (LBE). In embodiments, the computer (COMP), level sensor(LBP), and level control valve (LBP′) may be used in a control loop toregulate the amount of feed water (LAX) that is introduced to the steamdrum (LBE).

In embodiments, the steam drum (LBE) is connected to a lower steam drum(LBF) via a plurality of heat transfer conduit (LBG, LBH, LBI). Inembodiments, lower steam drum (LBF) is configured to discharge ablowdown (LBK) through a valve (LBN). In embodiments, the blowdown (LBK)includes suspended solids (LBL) and/or dissolved solids (LBM). Inembodiments, the suspended solids (LBL) include solids such as bacteria,silt and mud. In embodiments, the dissolved solids (LBM) may includeminerals, salts, metals, cations or anions dissolved in water. Inembodiments, the dissolved solids (LBM) include inorganic saltsincluding principally calcium, magnesium, potassium, sodium,bicarbonates, chlorides, and sulfates.

In embodiments, the condensate tank (LAP) also serves the purpose as awater tank (LAO) for accepting treated water (LAJ). Thus, treated water(LAJ) is added to the condensate tank (LAP) to make-up for water lossesin the system. A source of water (LAA) is made available to a series ofunit operations that are configured to improve the water. Inembodiments, the source of water (LAA) is passed through a filter (LAC),a packed bed (LAD) of adsorbent (LAE), a cation (LAF), an anion (LAG), amembrane (LAH), followed by another cation/anion (LAI) to result intreated water (LAJ).

The treated water (LAJ) is then provided to the condensate tank(LAP)/water tank (LAO) via a pump (LAK). In embodiments, the treatedwater (LAJ) that is transferred to the condensate tank (LAP)/water tank(LAO) via a pump (LAK) is passed through a valve (LAL). The valve (LAL)is equipped with a controller (LAM) that is configured to input oroutput a signal (XAM) to the computer (COMP). A quality sensor (LAN) isprovided as a quality control of the unit operations that are configuredto improve the water.

Within the interior (G14) of a mixing tank (G15), the water is mixedwith insects and biocatalyst. In embodiments, a cation (G39), an anion(G40), and a polishing unit (G41), are positioned on the water supplyconduit (G37) in between the third water treatment unit (G12) and thewater input (G38) of the mixing tank (G15). The polishing unit (G41) maybe any type of conceivable device to improve the water quality such asan ultraviolet unit, ozone unit, microwave unit, filter, a distillationsystem or the like.

FIG. 15:

FIG. 15 shows a simplistic diagram illustrating a plurality of feedingchambers (FC1, FC2, FC3) of an insect feeding module (2000) integratedwithin one common separator (300) of an insect evacuation module (3000).

FIG. 15 shows an insect feeding module (2000) comprised of threeseparate feeding chambers (FC1, FC2, FC3) including a first feedingchamber (FC1), second feeding chamber (FC2), and a third feeding chamber(FC3). Each feeding chamber (FC1, FC2, FC3) may include the non-limitingembodiments of those previously described or those described below. Itis well established that the claims of the patent serve an importantpublic notice function to potential competitors—enabling them to notonly determine what is covered, but also what is not covered—by thepatent. And a number of Federal Circuit decisions have emphasized theimportance of discerning the patentee's intent—as expressed in thespecification—in construing the claims of the patent. The presentdisclosure includes several independently meritorious inventive aspectsand advantages related feeding and evacuating insects by use of at leastone insect feeding module (2000) integrated at least one separator (300)of an insect evacuation module (3000) and to the notion that eachfeeding chamber (FC1, FC2, FC3) has a feeding chamber insect evacuationoutput (205A, 205B, 205C) that is connected to the separator (300) ofthe insect evacuation module (3000).

First Feeding Chamber (FC1)

The first feeding chamber (FC1) has a first feeding chamber insectevacuation output (205A) or a feeding chamber 1 insect evacuation port(1FC) that is in fluid communication with the insect and gas mixtureinput (303) of the separator (300). A first feeding chamber exit conduit(302A) is connected at one end to the first feeding chamber (FC1) and atanother and to a common entry conduit (CEC). The common entry conduit(CEC) is connected at one end to the first feeding chamber exit conduit(302A) and at another end to the insect and gas mixture input (303) ofthe separator (300). A feeding chamber 1 evacuation valve (VV1) ininterposed in the first feeding chamber exit conduit (302A). The feedingchamber 1 evacuation valve (VV1) is equipped with a with a controller(CV1) that is configured to input and output a signal (XV1) to thecomputer (COMP). The first feeding chamber exit conduit (302A) has afirst feeding chamber evacuation line first diameter (D1A) and a firstfeeding chamber evacuation line reducer (VR1) which merges into a firstfeeding chamber evacuation line second diameter (D1B). In embodiments,the first feeding chamber evacuation line first diameter (D1A) isgreater than the first feeding chamber evacuation line second diameter(D1B). In embodiments, the first feeding chamber evacuation line firstdiameter (D1A) is less than the first feeding chamber evacuation linesecond diameter (D1B).

In embodiments, the first feeding chamber evacuation line first diameter(D1A) ranges in size from: between about 1 inch and about 2 inches;between about 2 inches and about 3 inches; between about 3 inches andabout 4 inches; between about 4 inches and about 5 inches; between about5 inches and about 6 inches; between about 6 inches and about 7 inches;between about 7 inches and about 8 inches; between about 8 inches andabout 9 inches; between about 9 inches and about 10 inches; betweenabout 10 inches and about 11 inches; between about 11 inches and about12 inches; between about 12 inches and about 13 inches; between about 13inches and about 14 inches; between about 14 inches and about 15 inches;between about 15 inches and about 16 inches; between about 16 inches andabout 17 inches; between about 17 inches and about 18 inches; betweenabout 18 inches and about 19 inches; between about 19 inches and about20 inches; between about 20 inches and about 21 inches; between about 21inches and about 22 inches; between about 22 inches and about 23 inches;between about 23 inches and about 24 inches; between about 24 inches andabout 25 inches; between about 25 inches and about 26 inches; betweenabout 26 inches and about 27 inches; between about 27 inches and about28 inches; between about 28 inches and about 29 inches; between about 29inches and about 30 inches; between about 30 inches and about 31 inches;between about 31 inches and about 32 inches; between about 32 inches andabout 33 inches; between about 33 inches and about 34 inches; betweenabout 34 inches and about 35 inches; between about 35 inches and about36 inches; between about 36 inches and about 37 inches; between about 37inches and about 38 inches; between about 38 inches and about 39 inches;or, between about 39 inches and about 40 inches; between about 38 inchesand about 39 inches; between about 39 inches and about 40 inches;between about 40 inches and about 50 inches; between about 50 inches andabout 60 inches; between about 60 inches and about 70 inches; betweenabout 70 inches and about 80 inches; between about 80 inches and about90 inches; between about 90 inches and about 100 inches; between about100 inches and about 125 inches; between about 125 inches and about 150inches; or, between about 150 inches and about 200 inches.

In embodiments, the first feeding chamber evacuation line seconddiameter (D1B) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

In embodiments, the common entry conduit (CEC) ranges in size from:between about 1 inch and about 2 inches; between about 2 inches andabout 3 inches; between about 3 inches and about 4 inches; between about4 inches and about 5 inches; between about 5 inches and about 6 inches;between about 6 inches and about 7 inches; between about 7 inches andabout 8 inches; between about 8 inches and about 9 inches; between about9 inches and about 10 inches; between about 10 inches and about 11inches; between about 11 inches and about 12 inches; between about 12inches and about 13 inches; between about 13 inches and about 14 inches;between about 14 inches and about 15 inches; between about 15 inches andabout 16 inches; between about 16 inches and about 17 inches; betweenabout 17 inches and about 18 inches; between about 18 inches and about19 inches; between about 19 inches and about 20 inches; between about 20inches and about 21 inches; between about 21 inches and about 22 inches;between about 22 inches and about 23 inches; between about 23 inches andabout 24 inches; between about 24 inches and about 25 inches; betweenabout 25 inches and about 26 inches; between about 26 inches and about27 inches; between about 27 inches and about 28 inches; between about 28inches and about 29 inches; between about 29 inches and about 30 inches;between about 30 inches and about 31 inches; between about 31 inches andabout 32 inches; between about 32 inches and about 33 inches; betweenabout 33 inches and about 34 inches; between about 34 inches and about35 inches; between about 35 inches and about 36 inches; between about 36inches and about 37 inches; between about 37 inches and about 38 inches;between about 38 inches and about 39 inches; or, between about 39 inchesand about 40 inches; between about 38 inches and about 39 inches;between about 39 inches and about 40 inches; between about 40 inches andabout 50 inches; between about 50 inches and about 60 inches; betweenabout 60 inches and about 70 inches; between about 70 inches and about80 inches; between about 80 inches and about 90 inches; between about 90inches and about 100 inches; between about 100 inches and about 125inches; between about 125 inches and about 150 inches; or, between about150 inches and about 200 inches.

Second Feeding Chamber (FC2)

The second feeding chamber (FC2) has a second feeding chamber insectevacuation output (205B) or a feeding chamber 2 insect evacuation port(2FC) that is in fluid communication with the insect and gas mixtureinput (303) of the separator (300). A second feeding chamber exitconduit (302B) is connected at one end to the second feeding chamber(FC2) and at another and to a common entry conduit (CEC). The commonentry conduit (CEC) is connected at one end to the second feedingchamber exit conduit (302B) and at another end to the insect and gasmixture input (303) of the separator (300). A feeding chamber 2evacuation valve (VV2) in interposed in the second feeding chamber exitconduit (302B). The feeding chamber 2 evacuation valve (VV2) is equippedwith a with a controller (CV2) that is configured to input and output asignal (XV2) to the computer (COMP). The second feeding chamber exitconduit (302B) has a second feeding chamber evacuation line firstdiameter (D2A) and a second feeding chamber evacuation line reducer(VR2) which merges into a second feeding chamber evacuation line seconddiameter (D2B). In embodiments, the second feeding chamber evacuationline first diameter (D2A) is greater than the second feeding chamberevacuation line second diameter (D2B). In embodiments, the secondfeeding chamber evacuation line first diameter (D2A) is less than thesecond feeding chamber evacuation line second diameter (D2B).

In embodiments, the second feeding chamber evacuation line firstdiameter (D2A) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

In embodiments, the second feeding chamber evacuation line seconddiameter (D2B) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

Third Feeding Chamber (FC3)

The third feeding chamber (FC3) has a third feeding chamber insectevacuation output (205C) or a feeding chamber 3 insect evacuation port(2FC) that is in fluid communication with the insect and gas mixtureinput (303) of the separator (300). The third feeding chamber (FC3) hasa third feeding chamber insect evacuation output (205C) or a feedingchamber 3 insect evacuation port (3FC) that is in fluid communicationwith the insect and gas mixture input (303) of the separator (300). Athird feeding chamber exit conduit (302C) is connected at one end to thethird feeding chamber (FC3) and at another and to a common entry conduit(CEC). The common entry conduit (CEC) is connected at one end to thethird feeding chamber exit conduit (302C) and at another end to theinsect and gas mixture input (303) of the separator (300). A feedingchamber 3 evacuation valve (VV3) in interposed in the third feedingchamber exit conduit (302C). The feeding chamber 3 evacuation valve(VV3) is equipped with a with a controller (CV3) that is configured toinput and output a signal (XV3) to the computer (COMP). The thirdfeeding chamber exit conduit (302C) has a third feeding chamberevacuation line first diameter (D3A) and a third feeding chamberevacuation line reducer (VR3) which merges into a third feeding chamberevacuation line second diameter (D3B). In embodiments, the third feedingchamber evacuation line first diameter (D3A) is greater than the thirdfeeding chamber evacuation line second diameter (D3B). In embodiments,the third feeding chamber evacuation line first diameter (D3A) is lessthan the third feeding chamber evacuation line second diameter (D3B).

In embodiments, the third feeding chamber evacuation line first diameter(D3A) ranges in size from: between about 1 inch and about 2 inches;between about 2 inches and about 3 inches; between about 3 inches andabout 4 inches; between about 4 inches and about 5 inches; between about5 inches and about 6 inches; between about 6 inches and about 7 inches;between about 7 inches and about 8 inches; between about 8 inches andabout 9 inches; between about 9 inches and about 10 inches; betweenabout 10 inches and about 11 inches; between about 11 inches and about12 inches; between about 12 inches and about 13 inches; between about 13inches and about 14 inches; between about 14 inches and about 15 inches;between about 15 inches and about 16 inches; between about 16 inches andabout 17 inches; between about 17 inches and about 18 inches; betweenabout 18 inches and about 19 inches; between about 19 inches and about20 inches; between about 20 inches and about 21 inches; between about 21inches and about 22 inches; between about 22 inches and about 23 inches;between about 23 inches and about 24 inches; between about 24 inches andabout 25 inches; between about 25 inches and about 26 inches; betweenabout 26 inches and about 27 inches; between about 27 inches and about28 inches; between about 28 inches and about 29 inches; between about 29inches and about 30 inches; between about 30 inches and about 31 inches;between about 31 inches and about 32 inches; between about 32 inches andabout 33 inches; between about 33 inches and about 34 inches; betweenabout 34 inches and about 35 inches; between about 35 inches and about36 inches; between about 36 inches and about 37 inches; between about 37inches and about 38 inches; between about 38 inches and about 39 inches;or, between about 39 inches and about 40 inches; between about 38 inchesand about 39 inches; between about 39 inches and about 40 inches;between about 40 inches and about 50 inches; between about 50 inches andabout 60 inches; between about 60 inches and about 70 inches; betweenabout 70 inches and about 80 inches; between about 80 inches and about90 inches; between about 90 inches and about 100 inches; between about100 inches and about 125 inches; between about 125 inches and about 150inches; or, between about 150 inches and about 200 inches.

In embodiments, the third feeding chamber evacuation line seconddiameter (D3B) ranges in size from: between about 1 inch and about 2inches; between about 2 inches and about 3 inches; between about 3inches and about 4 inches; between about 4 inches and about 5 inches;between about 5 inches and about 6 inches; between about 6 inches andabout 7 inches; between about 7 inches and about 8 inches; between about8 inches and about 9 inches; between about 9 inches and about 10 inches;between about 10 inches and about 11 inches; between about 11 inches andabout 12 inches; between about 12 inches and about 13 inches; betweenabout 13 inches and about 14 inches; between about 14 inches and about15 inches; between about 15 inches and about 16 inches; between about 16inches and about 17 inches; between about 17 inches and about 18 inches;between about 18 inches and about 19 inches; between about 19 inches andabout 20 inches; between about 20 inches and about 21 inches; betweenabout 21 inches and about 22 inches; between about 22 inches and about23 inches; between about 23 inches and about 24 inches; between about 24inches and about 25 inches; between about 25 inches and about 26 inches;between about 26 inches and about 27 inches; between about 27 inches andabout 28 inches; between about 28 inches and about 29 inches; betweenabout 29 inches and about 30 inches; between about 30 inches and about31 inches; between about 31 inches and about 32 inches; between about 32inches and about 33 inches; between about 33 inches and about 34 inches;between about 34 inches and about 35 inches; between about 35 inches andabout 36 inches; between about 36 inches and about 37 inches; betweenabout 37 inches and about 38 inches; between about 38 inches and about39 inches; or, between about 39 inches and about 40 inches; betweenabout 38 inches and about 39 inches; between about 39 inches and about40 inches; between about 40 inches and about 50 inches; between about 50inches and about 60 inches; between about 60 inches and about 70 inches;between about 70 inches and about 80 inches; between about 80 inches andabout 90 inches; between about 90 inches and about 100 inches; betweenabout 100 inches and about 125 inches; between about 125 inches andabout 150 inches; or, between about 150 inches and about 200 inches.

FIG. 15 describes an Insect Production Superstructure System (IPSS) thatinsect feeding module (2000) provides insects contained therein to beable to

Insect Mobility

Large scale insect production systems must be designed responsibly tomake sure that the insects are freed from hunger, thirst, discomfort,pain, injury, disease, fear and distress. Three feeding chambers (FC1,FC2, FC3) are shown in FIG. 15 and the egg-laying insects presenttherein may freely travel from one feeding chamber to another.

The plurality of feeding chambers and a passageways therebetweenencourage egg-laying insects therein to express normal behavior byenabling mobility and relocation to a more suitable living environment.An insect may decide to up and relocate for any reason it chooses or noreason at all. In the event that one breeding chamber lacks sufficientamounts of enhanced feedstock, or is over-crowded, or contains diseasedor cannibalistic insects, the insects may relocate to another feedingchamber to alleviate their discomfort, pain, injury, disease, and fearand distress.

FIG. 15 describes a portion of an Insect Production SuperstructureSystem (IPSS) that permits insects to have mobility and the opportunityto choose between different possible courses of action. Herein aredisclosed advancements and better solutions that meet new requirements,unarticulated needs, or existing market needs in maximizing insectwelfare, maximizing insect output on a minimal physical outlay, andbenefit of large groups of people a high-value animal protein.

The first feeding chamber (FC1) is connected to the second feedingchamber (FC2) via a chamber 2 to chamber 1 transfer line (TL21). Thefirst feeding chamber (FC1) is also connected to the third feedingchamber (FC3) via a chamber 3 to chamber 1 transfer line (TL31). Thefirst feeding chamber (FC1) is also connected to the any one of aplurality of breeding chambers (BC, BC1, BC2. BC3) via a chamber 1breeding chamber transfer line (TLBC1) which is elaborated upon more inFIGS. 16 and 17.

The second feeding chamber (FC2) is connected to the first feedingchamber (FC1) via a chamber 1 to chamber 2 transfer line (TL12). Thesecond feeding chamber (FC2) is also connected to the third feedingchamber (FC3) via a chamber 3 to chamber 2 transfer line (TL32). Thesecond feeding chamber (FC2) is also connected to the any one of aplurality of breeding chambers (BC, BC1, BC2. BC3) via a chamber 2breeding chamber transfer line (TLBC2) which is elaborated upon more inFIGS. 16 and 17.

The third feeding chamber (FC3) is connected to the first feedingchamber (FC1) via a chamber 1 to chamber 3 transfer line (TL13). Thethird feeding chamber (FC3) is also connected to the second feedingchamber (FC2) via a chamber 2 to chamber 3 transfer line (TL23). Thethird feeding chamber (FC3) is also connected to the any one of aplurality of breeding chambers (BC, BC1, BC2. BC3) via a chamber 3breeding chamber transfer line (TLBC3) which is elaborated upon more inFIGS. 16 and 17.

In embodiments, the insect feeding chamber grows insects in the presenceof music. In embodiments, the cannabis plants grow in the presence ofmusic. In embodiments, the cannabis plants grow and insects in thepresence of music. In embodiments, the cannabis plants (as disclosed inVolume II) are grown within an interior of an enclosure wherein musicplays within the interior of the enclosure. In embodiments, thepsilocybin mushrooms are grown in the presence of music. In embodiments,the insect feeding chamber operates with music playing within it. Inembodiments, the insects are grown within an interior of an enclosurewherein music plays within the interior of the enclosure. Inembodiments, the insect breeding chamber operates with music playingwithin it. In embodiments, the insects are incubated within an interiorof an enclosure wherein music plays within the interior of theenclosure. In embodiments, the insect eggs are incubated within aninterior of an enclosure wherein music plays within the interior of theenclosure.

In embodiments, the music includes one or more types of music selectedfrom the group consisting of: alternative music, blues music, classicalmusic, vaudeville music, commercials music, country music, dance music,easy listening music, electronic music, enka music, french pop music,german folk music, german pop music, fitness & workout music, hip-hopmusic, rap music, holiday music, indie pop music, industrial music,inspirational music, Christian music, gospel music, instrumental music,jazz music, karaoke music, kayokyoku music, latin music, live music, alive marching band, marching band music, new age music, opera music, popmusic, r&b music, soul music, reggae music, rock music,singer/songwriter music, soundtrack music, spoken word, tex-mex music,tejano music, techno music, trance music, vocal music, world music, andcombinations thereof.

In embodiments, the music includes acoustics. In embodiments, theacoustics includes a beat. In embodiments, the beat includes aninterference pattern between two sounds of slightly differentfrequencies. In embodiments, the beat includes a periodic variation involume whose rate is the difference of the two frequencies.

In embodiments, the music includes acoustics include a frequency rangingfrom one or more frequencies selected from the group consisting of: 5.00(hertz) hz to 5.25 hz, 5.25 hz to 5.50 hz, 5.50 hz to 5.75 hz, 5.75 hzto 6.00 hz, 6.00 hz to 6.25 hz, 6.25 hz to 6.50 hz, 6.50 hz to 6.75 hz,6.75 hz to 7.00 hz, 7.00 hz to 7.25 hz, 7.25 hz to 7.50 hz, 7.50 hz to7.75 hz, 7.75 hz to 8.00 hz, 8.00 hz to 8.25 hz, 8.25 hz to 8.50 hz,8.50 hz to 8.75 hz, 8.75 hz to 9.00 hz, 9.00 hz to 9.25 hz, 9.25 hz to9.50 hz, 9.50 hz to 9.75 hz, 9.75 hz to 10 hz, 10 hz to 12 hz, 12 hz to14 hz, 14 hz to 16 hz, 16 hz to 18 hz, 18 hz to 20 hz, 20 hz to 30 hz,30 hz to 40 hz, 40 hz to 50 hz, 50 hz to 60 hz, 60 hz to 70 hz, 70 hz to80 hz, 80 hz to 90 hz, 90 hz to 100 hz, 100 hz to 200 hz, 200 hz to 300hz, 300 hz to 400 hz, 400 hz to 500 hz, 500 hz to 600 hz, 600 hz to 700hz, 700 hz to 800 hz, 800 hz to 900 hz, 900 hz to 1000 hz, 1000 hz to2000 hz, 2000 hz to 3000 hz, 3000 hz to 4000 hz, 4000 hz to 5000 hz,5000 hz to 6000 hz, 6000 hz to 7000 hz, 7000 hz to 8000 hz, 8000 hz to9000 hz, 9000 hz to 10000 hz, 10000 hz to 20000 hz, 20000 hz to 30000hz, 30000 hz to 40000 hz, or 40000 hz to 50000 hz.

In embodiments, the insect feeding chamber operates at a sound frequencyranging from one or more frequencies selected from the group consistingof: 5.00 (hertz) hz to 5.25 hz, 5.25 hz to 5.50 hz, 5.50 hz to 5.75 hz,5.75 hz to 6.00 hz, 6.00 hz to 6.25 hz, 6.25 hz to 6.50 hz, 6.50 hz to6.75 hz, 6.75 hz to 7.00 hz, 7.00 hz to 7.25 hz, 7.25 hz to 7.50 hz,7.50 hz to 7.75 hz, 7.75 hz to 8.00 hz, 8.00 hz to 8.25 hz, 8.25 hz to8.50 hz, 8.50 hz to 8.75 hz, 8.75 hz to 9.00 hz, 9.00 hz to 9.25 hz,9.25 hz to 9.50 hz, 9.50 hz to 9.75 hz, 9.75 hz to 10 hz, 10 hz to 12hz, 12 hz to 14 hz, 14 hz to 16 hz, 16 hz to 18 hz, 18 hz to 20 hz, 20hz to 30 hz, 30 hz to 40 hz, 40 hz to 50 hz, 50 hz to 60 hz, 60 hz to 70hz, 70 hz to 80 hz, 80 hz to 90 hz, 90 hz to 100 hz, 100 hz to 200 hz,200 hz to 300 hz, 300 hz to 400 hz, 400 hz to 500 hz, 500 hz to 600 hz,600 hz to 700 hz, 700 hz to 800 hz, 800 hz to 900 hz, 900 hz to 1000 hz,1000 hz to 2000 hz, 2000 hz to 3000 hz, 3000 hz to 4000 hz, 4000 hz to5000 hz, 5000 hz to 6000 hz, 6000 hz to 7000 hz, 7000 hz to 8000 hz,8000 hz to 9000 hz, 9000 hz to 10000 hz, 10000 hz to 20000 hz, 20000 hzto 30000 hz, 30000 hz to 40000 hz, or 40000 hz to 50000 hz.

Insect Evacuation

The insect evacuation module (3000) is configured to pull a vacuum oneach one of the plurality of insect feeding chambers at any given timeto evacuate the insects contained therein. A computer (COMP) may beprogrammed to control the operation of the insect evacuation module(3000) to be able to systematically apply a vacuum on any one separateor individually of either of the first feeding chamber (FC1), secondfeeding chamber (FC2), or third feeding chamber (FC3).

The level of the vacuum by the insect evacuation fan (312) may vary.Alternatively, instead of a fan, a vacuum pump, steam jet ejector,pneumatic vacuum, eductor, or any conceivable vacuuming means to realizethe end to pull a vacuum on any number of plurality of feeding chambers(FC1, FC2, FC3) at any given time may be used. At times, it is importantto be able to only draw a vacuum on only one of the feeding chambers atany given time depending upon how far along in the insect growth stageany given feeding chamber (FC1, FC2, FC3) is at. For example, bymeasuring the pressure drop across each of the network of cellscontained within any given feeding chamber (FC1, FC2, FC3), it may bedetermined that it is desirable to only evacuated the insects from say,for example, feeding chamber 1 (FC1) while leaving the other two feedingchambers (FC2, FC3) to remain unchanged to promote stable insect growth.To achieve this end, the computer (COMP) will send a signal (XV1) toonly the feeding chamber 1 evacuation valve (VV1) on the first feedingchamber (FC1) to evacuate the contents therein.

A common insect evacuation pressure sensor (PT10) is installed on thecommon entry conduit (CEC), or alternatively may be installed on anyplurality number of separators (S1, S1, S3). The common insectevacuation pressure sensor (PT10) is configured to input a signal (XT10)to the computer (COMP). A common insect evacuation vent line (VRL) isconnected at one end to the common entry conduit (CEC) and connected atanother end to a header vacuum vent valve (VV0). The header vacuum ventvalve (VV0) is interposed on the common insect evacuation vent line(VRL) and is in fluid communication with both the insect evacuation fan(312) and each one of the plurality of insect feeding chambers (FC1,FC2, FC3). The header vacuum vent valve (VV0) is equipped with acontroller (CV0) that is configured to input and output a signal (XV0)to the computer (COMP). At least one common insect evacuation linereducer (VR0) is interposed on the common insect evacuation vent line(VRL).

The header vacuum vent valve (VV0) is configured to be able to controlthe level of vacuum pulled on a feeding chamber (FC1, FC2, FC3). In theevent that a deep vacuum needs to be pulled to evacuate a feedingchamber that has reached its maximum or desired insect capacity, theheader vacuum vent valve (VV0) may be operatively included in a controlloop while integrated with (i) the common insect evacuation pressuresensor (PT10), and (ii) the controller (316) of the fan motor (314) ofthe insect evacuation fan (312). For example, if a deep vacuum needs tobe pulled on, say feeding chamber 1 (FC1), while leaving the otherfeeding chambers unchanged, the header vacuum vent valve (VV0) mayremain in the closed position to permit the insect evacuation fan (312)to completely draw down the pressure in the feeding chamber 1 (FC1) topull an insect and gas mixture having an insect portion and a gasportion through the first feeding chamber insect evacuation output(205A) and common entry conduit (CEC). If the header vacuum vent valve(VV0) is then opened, or modulated, by any given percentage, it willincrease the gas portion of the insect and gas mixture flowing into theseparator (300) and thus increase the pressure in the feeding chamber(FC1) since not as deep of a vacuum will be pulled on the feedingchamber (FC1). A header vacuum vent valve (VV0) may be able to aide inthe separation of insects and gas within any plurality of separators(S1, S2, S3) contained within the insect evacuation module (3000) byproviding a predictable and consistent inlet velocity at the inlet ofany number of any give plurality of separators (S1, S2, S3).

In embodiments, the egg-laying insects may be evacuated from anyplurality of feeding chambers (FC1, FC2, FC3) by applying a vacuum witha velocity pressure range from: between about 0.001 inches of water toabout 0.002 inches of water; between about 0.002 inches of water toabout 0.003 inches of water; between about 0.003 inches of water toabout 0.006 inches of water; between about 0.006 inches of water toabout 0.012 inches of water; between about 0.012 inches of water toabout 0.024 inches of water; between about 0.024 inches of water toabout 0.050 inches of water; between about 0.050 inches of water toabout 0.075 inches of water; between about 0.075 inches of water toabout 0.150 inches of water; between about 0.150 inches of water toabout 0.300 inches of water; between about 0.300 inches of water toabout 0.450 inches of water; between about 0.450 inches of water toabout 0.473 inches of water; between about 0.473 inches of water toabout 0.496 inches of water; between about 0.496 inches of water toabout 0.521 inches of water; between about 0.521 inches of water toabout 0.547 inches of water; between about 0.547 inches of water toabout 0.574 inches of water; between about 0.574 inches of water toabout 0.603 inches of water; between about 0.603 inches of water toabout 0.633 inches of water; between about 0.633 inches of water toabout 0.665 inches of water; between about 0.665 inches of water toabout 0.698 inches of water; between about 0.698 inches of water toabout 0.733 inches of water; between about 0.733 inches of water toabout 0.770 inches of water; between about 0.770 inches of water toabout 0.808 inches of water; between about 0.808 inches of water toabout 0.849 inches of water; between about 0.849 inches of water toabout 0.891 inches of water; between about 0.891 inches of water toabout 0.936 inches of water; between about 0.936 inches of water toabout 0.982 inches of water; between about 0.982 inches of water toabout 1.031 inches of water; between about 1.031 inches of water toabout 1.083 inches of water; between about 1.083 inches of water toabout 1.137 inches of water; between about 1.137 inches of water toabout 1.194 inches of water; between about 1.194 inches of water toabout 1.254 inches of water; between about 1.254 inches of water toabout 1.316 inches of water; between about 1.316 inches of water toabout 1.382 inches of water; between about 1.382 inches of water toabout 1.451 inches of water; between about 1.451 inches of water toabout 1.524 inches of water; between about 1.524 inches of water toabout 2.286 inches of water; between about 2.286 inches of water toabout 3.429 inches of water; between about 3.429 inches of water toabout 5.143 inches of water; between about 5.143 inches of water toabout 7.715 inches of water; between about 7.715 inches of water toabout 11.572 inches of water; between about 11.572 inches of water toabout 17.358 inches of water; between about 17.358 inches of water toabout 26.037 inches of water; between about 26.037 inches of water toabout 39.055 inches of water; between about 39.055 inches of water toabout 58.582 inches of water; between about 58.582 inches of water toabout 87.873 inches of water; between about 87.873 inches of water toabout 131.810 inches of water; between about 131.810 inches of water toabout 197.715 inches of water; between about 197.715 inches of water toabout 296.573 inches of water; or, between about 296.573 inches of waterto about 400 inches of water.

In embodiments, the egg-laying insects may be evacuated from anyplurality of feeding chambers (FC1, FC2, FC3) by applying a velocityfrom: between about 0.05 feet per second to between about 0.10 feet persecond; 0.10 feet per second to between about 0.15 feet per second; 0.15feet per second to between about 0.25 feet per second; 0.25 feet persecond to between about 0.40 feet per second; 0.40 feet per second tobetween about 0.65 feet per second; 0.65 feet per second to betweenabout 1.05 feet per second; 1.05 feet per second to between about 1.70feet per second; 1.70 feet per second to between about 2.75 feet persecond; 2.75 feet per second to between about 3.09 feet per second; 3.09feet per second to between about 3.64 feet per second; 3.64 feet persecond to between about 4.26 feet per second; 4.26 feet per second tobetween about 4.99 feet per second; 4.99 feet per second to betweenabout 5.84 feet per second; 5.84 feet per second to between about 6.83feet per second; 6.83 feet per second to between about 8.00 feet persecond; 8.00 feet per second to between about 9.37 feet per second; 9.37feet per second to between about 10.97 feet per second; 10.97 feet persecond to between about 12.84 feet per second; 12.84 feet per second tobetween about 15.04 feet per second; 15.04 feet per second to betweenabout 17.61 feet per second; 17.61 feet per second to between about20.61 feet per second; 20.61 feet per second to between about 24.14 feetper second; 24.14 feet per second to between about 28.26 feet persecond; 28.26 feet per second to between about 33.08 feet per second;33.08 feet per second to between about 38.74 feet per second; 38.74 feetper second to between about 45.35 feet per second; 45.35 feet per secondto between about 53.10 feet per second; 53.10 feet per second to betweenabout 62.17 feet per second; 62.17 feet per second to between about72.79 feet per second; 72.79 feet per second to between about 85.23 feetper second; 85.23 feet per second to between about 99.78 feet persecond; 99.78 feet per second to between about 116.83 feet per second;116.83 feet per second to between about 136.79 feet per second; 136.79feet per second to between about 160.15 feet per second; 160.15 feet persecond to between about 187.51 feet per second; 187.51 feet per secondto between about 219.54 feet per second; 219.54 feet per second tobetween about 257.04 feet per second; 257.04 feet per second to betweenabout 300.95 feet per second; 300.95 feet per second to between about352.36 feet per second; 352.36 feet per second to between about 412.55feet per second; 412.55 feet per second to between about 483.02 feet persecond; 483.02 feet per second to between about 565.53 feet per second;565.53 feet per second to between about 662.13 feet per second; 662.13feet per second to between about 775.24 feet per second; 775.24 feet persecond to between about 907.66 feet per second; 907.66 feet per secondto between about 1062.71 feet per second; 1062.71 feet per second tobetween about 1244.24 feet per second; 1244.24 feet per second tobetween about 1456.78 feet per second; or, 1456.78 feet per second tobetween about 1500.00 feet per second.

FIG. 16:

FIG. 16 shows a simplistic diagram illustrating a plurality ofseparators (S1, S2, S3) integrated with one common feeding chamber(FC1), and wherein the feeding chamber (FC1) and second separator (S2)are in fluid communication with one common breeding chamber (BC), andwherein the breeding chamber (BC) is in fluid communication with onecommon breeding material and insect separator (SEPIA), and wherein thebreeding material and insect separator (SEPIA) is in fluid communicationwith at least one of a plurality of feeding chambers (FC1, FC2, FC3).

FIG. 16 shows a simplistic diagram illustrating a plurality ofseparators (S1, S2, S3) integrated with one common feeding chamber(FC1), and wherein the feeding chamber (FC1) and second separator (S2)are in fluid communication with one common breeding chamber (BC), andwherein the breeding chamber (BC) is in fluid communication with onecommon breeding material and insect separator (SEPIA), and wherein thebreeding material and insect separator (SEPIA) is in fluid communicationwith at least one of a plurality of feeding chambers (FC1, FC2, FC3).

FIG. 16 shows a portion of the Insect Production Superstructure System(IPSS) including an insect feeding module (2000), an insect evacuationmodule (3000), an insect breeding module (4000), and hatched insectseparation module (5000). The insect feeding module (2000) is configuredto feed the enhanced feedstock from the enhanced feedstock mixing module(1000) and grow insects so that egg-laying insects may in turn lay eggs.The insect evacuation module (3000) is configured to remove insects,residual enhanced feedstock, particulates including insect exoskeletonfrom the any of a plurality of insect feeding modules (2000, 2000A,200B, 2000C). The insect breeding module (4000) is configured to removeeggs from the insect feeding module (2000) for incubation over atemperature and humidity controlled duration of time to formhatched-insects. The hatched insect separation module (5000) isconfigured to separate the hatched-insects and breeding material fromthe insect breeding module (4000) and then distribute the separatedbreeding material to any one of the plurality of the insect feedingmodules (2000, 2000A, 2000B, 2000C). In embodiments, the insects areincubated within an interior of an enclosure in the absence of light. Inembodiments, the insects are incubated within an interior of anenclosure are photophobic, wherein the insects are sensitive to light,and possess an intolerance of light.

FIG. 16 shows an insect feeding module (2000) including one feedingchamber (FC1) integrated with an insect evacuation module (3000)comprised of a first separator (51), second separator (S2), and a thirdseparator (S3). FIG. 16 shows the first separator (51) and secondseparator (S2) as cyclones. FIG. 16 also shows the third separator (S3)as a filter. It is to be noted that the embodiment of FIG. 16 isnon-limiting and shall not be construed to limit the disclosure in anyway. Any number of separators (51, S2, S3) may be employed and anypermutation or combination of separation unit operations or devices maybe used so long as insect portion (304A) is separated from a gas portion(304B) of an insect and gas mixture (304).

FIG. 16 shows the first separator (S1) as a first insect coarseseparator (S1A), the second separator (S2) as a second insect fineseparator (S2A), and the third separator (S3) as a particulate separator(S3A). The first insect coarse separator (S1A) is configured to remove aportion of the insect portion (304A) separated from the gas portion(304B) of an insect and gas mixture (304). The second insect fineseparator (S2A) is configured to remove insects smaller than the insectsseparated in the first insect coarse separator (S1A). The particulateseparator (S3A) is configured to remove particulates such as remnants ofenhanced feedstock, or fine polymer particulate, for example, not onlyincluding pieces of portions of insect exoskeleton. The particulateseparator (S3A) is in fluid communication with the polymer distributionmodule (1D) and is configured to transfer a portion of the separatedparticulate to the polymer tank (1D2) as polymer (1D1).

First Separator (S1), First Insect Coarse Separator (S1A)

The first insect coarse separator (S1A) has a first insect coarseseparator input (S1A1) that is in fluid communication with the firstfeeding chamber insect evacuation output (205A) of the first feedingchamber (FC1) via a first feeding chamber exit conduit (302A). The firstinsect coarse separator (S1A) is configured to accept an insect and gasmixture (304) from the first feeding chamber (FC1), separate a portionof the insects from the gas and output a first insect-depleted gasstream (355) via a coarse separator gas and insect mixture output (356).

The first separator (S1) is equipped with a first dipleg (357), a firstseparator conveyor (358), and a first separator valve (361) interposedon the first dipleg (357). A first separated insect stream (360) isrouted down the first dipleg (357), through the first separator valve(361) and into the first separator conveyor (358). In embodiments, thefirst separator conveyor (358) is a compression screw (359) which servesto instantly kill insects by compressing them. The first separatedinsect stream (360) may in turn be sent to a grinder (1250) within aninsect grinding module via a first separated insect stream input (371).In other embodiments, the first separated insect stream (360) may besent to a pathogen removal unit (1550) within a pathogen removal module,or to a within a lipid extraction unit (1501) lipid extraction module.

Second Separator (S2), Second Insect Fine Separator (S2A)

The second insect fine separator (S2A) has a second insect fineseparator input (S2A1) that is in fluid communication with the coarseseparator gas and insect mixture output (356) of the first insect coarseseparator (S1A). The second insect fine separator (S2A) is configured toaccept a first insect-depleted gas stream (355) from the first insectcoarse separator (S1A), separate a portion of the insects from the gasand output a second insect-depleted gas stream (362) via a fineseparator gas and particulate mixture output (363).

The second separator (S2) is equipped with a second dipleg (364), asecond separator conveyor (365), and a second separator valve (368)interposed on the second dipleg (364). A second separated insect stream(360) is routed down the second dipleg (364), through the secondseparator valve (368) and into the second separator conveyor (365). Inembodiments, the second separator conveyor (365) is a compression screw(366) which serves to instantly kill insects by compressing them.

In embodiments, the second separator conveyor (365) is a not acompression screw (366) but instead routes the second separated insectstream (367) to the to a breeding chamber (BC) via a breeding chamberfine separated insect portion input (375). In embodiments, the secondseparator conveyor (365) is a not a compression screw (366) but insteadroutes the second separated insect stream (367) to a plurality of otherdestinations such as to the grinder (1250), pathogen removal unit(1550), or lipid extraction unit (1501). The second separated insectstream (367) may be sent to a grinder (1250) within an insect grindingmodule via a first separated insect stream input (371). In otherembodiments, the second separated insect stream (367) may be sent to apathogen removal unit (1550) within a pathogen removal module, or to awithin a lipid extraction unit (1501) lipid extraction module.

Third Separator (S3), Particulate Separator (S3A)

The particulate separator (S3A) has a particulate separator input (S3A1)that is in fluid communication with the fine separator gas andparticulate mixture output (363) of the second insect fine separator(S2A). The particulate separator (S3A) is configured to accept a secondinsect-depleted gas stream (362) from the second insect fine separator(S2A), separate a portion of the particulates from the gas and output aparticulate-depleted gas stream (369) to the insect evacuation fan(312).

The insect evacuation fan (312) is in fluid with the breeding chamber(BC) via a breeding chamber exhaust input (376) and is configured todischarge the exhaust (377) into the breeding chamber (BC). Inembodiments, the separated insect conveyor (328) of the third separator(S3) particulate separator (S3A) is in fluid communication with thepolymer distribution module (1D) and is configured to transfer a portionof the separated particulate stream (370) to the polymer tank (1D2) aspolymer (1D1).

Insect Breeding Module (4000)

FIG. 16 shows the insect feeding module (2000) integrated with theinsect breeding module (4000). The insect breeding module (4000) isconfigured to remove eggs from the insect feeding module (2000) forincubation over a temperature and humidity controlled duration of timeto form hatched-insects.

The insect breeding module (4000) contains a breeding chamber (BC). FIG.16 shows one breeding chamber (BC) portrayed as breeding chamber 1(BC1). It is to be noted that FIG. 16 shows a first feeding chamber(FC1) connected to a breeding chamber 1 (BC1) via a feeding chamber 1egg-laden breeding material transfer line (R1).

The feeding chamber 1 egg-laden breeding material transfer line (R1) isconnected at one end to the first feeding chamber (FC1) via a conveyoroutput (249) and at another end to breeding chamber 1 (BC1) via afeeding chamber 1 breeding chamber 1 input (BC1A). The feeding chamber 1egg-laden breeding material transfer line (R1) is configured to transferan egg-laden breeding material (250) to the interior (BCIN) of breedingchamber 1 (BC1). In embodiments, the interior (BCIN) of the breedingchamber 1 (BC1) contains a tiered plurality of conveyors that include atleast an upper and a lower conveyor wherein egg-laden breeding material(250) is transferred from conveyors spaced apart from one another in avertical orientation to permit sufficient time to incubate the eggscontained within the egg-laden breeding material (250) to hatch insects.

FIG. 16 shows egg-laden breeding material (250) being transferred to theinterior (BCIN) of the breeding chamber 1 (BC1) where it is firstelevated via a first conveyor transfer unit (XY1A) to the first conveyorheight (CH1A) of a first conveyor (CY1A) operating in a clockwise motionof operation.

The first conveyor (CY1A) is positioned at a vertical height above atleast one other conveyor. FIG. 16 shows seven conveyors (CY1A, CY2A,CY3A, CY4A, CYSA, CY6A, CY7A) and the first conveyor (CY1A) ispositioned at a vertical height above each one of a second conveyor(CY2A), third conveyor (CY3A), fourth conveyor (CY4A), fifth conveyor(CYSA), sixth conveyor (CY6A), and seventh conveyor (CY7A). The secondconveyor (CY2A) is positioned at a vertical height above each one of athird conveyor (CY3A), fourth conveyor (CY4A), fifth conveyor (CYSA),sixth conveyor (CY6A), and seventh conveyor (CY7A). The third conveyor(CY3A) is positioned at a vertical height above each one of a fourthconveyor (CY4A), fifth conveyor (CYSA), sixth conveyor (CY6A), andseventh conveyor (CY7A). The fourth conveyor (CY4A) is positioned at avertical height above each one of a fifth conveyor (CY5A), sixthconveyor (CY6A), and seventh conveyor (CY7A). The fifth conveyor (CY5A)is positioned at a vertical height above each one of a sixth conveyor(CY6A), and seventh conveyor (CY7A). The sixth conveyor (CY6A) ispositioned at a vertical height above the seventh conveyor (CY7A).

The first conveyor (CY1A) is installed at a first conveyor height (CH1A)above the second conveyor (CY2A). The second conveyor (CY2A) isinstalled at a second conveyor height (CH2A) above the third conveyor(CY3A). The third conveyor (CY3A) is installed at a third conveyorheight (CH3A) above the fourth conveyor (CY4A). The fourth conveyor(CY4A) is installed at a fourth conveyor height (CH4A) above the fifthconveyor (CY5A). The fifth conveyor (CY5A) is installed at a fifthconveyor height (CH5A) above the sixth conveyor (CY6A). The sixthconveyor (CY6A) is installed at a sixth conveyor height (CH6A) above theseventh conveyor (CY7A).

The seventh conveyor (CY7A) is installed at a seventh conveyor height(CH7A) below all other conveyors (CY1A, CY2A, CY3A, CY4A, CY5A, CY6A).FIG. 16 shows the first conveyor (CY1A), third conveyor (CY3A), fifthconveyor (CY5A), seventh conveyor (CY7A) all configured to operate in aclockwise motion of operation. FIG. 16 shows the second conveyor (CY2A),fourth conveyor (CY4A), sixth conveyor (CY6A), all configured to operatein a counter-clockwise motion of operation.

A conveyor 1 to conveyor 2 transfer unit (XY2A) is configured totransfer the egg-laden breeding material from the first conveyor (CY1A)to the second conveyor (CY2A). The conveyor 2 to conveyor 3 transferunit (XY3A) is configured to transfer the egg-laden breeding materialfrom the second conveyor (CY2A) to the third conveyor (CY3A). Theconveyor 3 to conveyor 4 transfer unit (XY4A) is configured to transferthe egg-laden breeding material from the third conveyor (CY3A) to thefourth conveyor (CY4A). The conveyor 4 to conveyor 5 transfer unit(XY5A) is configured to transfer the egg-laden breeding material fromthe fourth conveyor (CY4A) to the fifth conveyor (CY5A). The conveyor 5to conveyor 6 transfer unit (XY6A) is configured to transfer theegg-laden breeding material, and perhaps hatched insects, from the fifthconveyor (CY5A) to the sixth conveyor (CY6A). The conveyor 6 to conveyor7 transfer unit (XY7A) is configured to transfer the egg-laden breedingmaterial, and perhaps hatched insects, from the sixth conveyor (CY6A) tothe seventh conveyor (CY7A). The seventh conveyor (CY7A) is configuredto transfer the hatched insects and breeding material from the feedingchamber 1 breeding chamber output (BC1B) of the interior (BCIN) of thebreeding chamber (BC) to the interior (SIN1) of the breeding materialand insect separator (SEPIA) contained within the hatched insectseparation module (5000).

Hatched Insect Separation Module (5000)

FIG. 16 shows the hatched insect separation module (5000) equipped witha breeding material and insect separator (SEPIA) and a breeding materialtank (500). The breeding material and insect separator (SEPIA) includesan interior (SIN1), a separator input (1SEPA), a separator materialoutput (1SEPB), and a separator insect output (1SEPC). The breedingmaterial and insect separator (SEPIA) is connected to breeding chamber 1(BC1) via a breeding chamber 1 hatched egg and breeding materialtransfer line (U1). The breeding chamber 1 hatched egg and breedingmaterial transfer line (U1) is connected at one end to the breedingchamber 1 (BC1) via a feeding chamber 1 breeding chamber output (BC1B)and connected at another end to the breeding material and insectseparator (SEPIA) via a separator input (1SEPA).

The separator input (1SEPA) is configured to accept hatched insects andbreeding material from the seventh conveyor (CY7A) of breeding chamber 1(BC1), and separate hatched insects (400) from the breeding material(523). The separator insect output (1SEPC) is configured to dischargehatched insects (400) from the interior (SIN1) of the breeding materialand insect separator (SEPIA) and route the hatched insects (400) toeither one of a plurality of feeding chambers (FC1, FC2, FC3) via aseparator hatched insect transfer line (01). Specifically, separatorinsect output (1SEPC) is configured to discharge hatched insects (400)first feeding chamber (FC1) via a separator feeding chamber 1 transferline (011), or to the second feeding chamber (FC2) via a separatorfeeding chamber 2 transfer line (012), or to the third feeding chamber(FC3) via a separator feeding chamber 3 transfer line (013). Hatchedinsects (400) transferred from the hatched insect separation module(5000) to the insect feeding module (2000) are made available to thefirst feeding chamber (FC1) via a separator feeding chamber 1 transferline (011) and a chamber 1 breeding chamber transfer line (TLBC1).

Breeding material (523) separated from the hatched insects (400) withinthe interior (SIN1) of the breeding material and insect separator(SEPIA) is routed to the interior (501) of a breeding material tank(500) via a separator material output (1SEPB). The breeding material(523) separated from the hatched insects (400) within the interior(SIN1) of the breeding material and insect separator (SEP1A) may becharacterized as an egg-depleted material (518) since eggs wereincubated to form hatched insects (400). A material transfer line (522)is connected at one end to the separator material output (1SEPB) of thebreeding material and insect separator (SEPIA) and connected at anotherend to the breeding material input (502) of the breeding material tank(500). An egg-depleted material transfer conveyor (519) may beinterposed in the material transfer line (522) in between the breedingmaterial and insect separator (SEPIA) and the breeding material tank(500).

The breeding material tank (500) has an interior (501), a breedingmaterial input (502), and a breeding material output (510). The breedingmaterial tank (500) also has a top section (503), a bottom section(506), and an interior (501) defined by at least one side wall (507). Abreeding material screw conveyor (508) is located at the bottom section(506) and configured to transfer breeding material to either one of aplurality of feeding chambers (FC1, FC2, FC3) via a breeding materialtransfer line (511). The breeding material transfer line (511) isconnected at one end to any one of a plurality of feeding chambers (FC1,FC2, FC3) and connected at another end to the breeding material screwconveyor (508) via a breeding material output (510). The breedingmaterial screw conveyor (508) is equipped with a breeding material screwconveyor motor (512), controller (513), and is configured to input andoutput a signal (514) to the computer (COMP).

FIG. 16A:

FIG. 16A shown one embodiment of a plurality of separators (KGA, KGB,KGC) that are configured to pull a vacuum on a plurality of insectfeeding chambers (FC1, FC2, FC3) and separate large insects (KGG), smallinsects (KGH), and particulates (KGI) therefrom while returning thesmall insects (KGH) back to the plurality of insect feeding chambers(FC1, FC2, FC3).

A fan (KGM) pulls a vacuum on the first feeding chamber (FC1), secondfeeding chamber (FC2), and third feeding chamber (FC3) through aparticulate separator (KGC), small insect separator (KGB), and a largeinsect separator (KGA). A large insect-small insect-particulate-gasmixture (KGJ) are evacuated from the first feeding chamber (FC1), secondfeeding chamber (FC2), third feeding chamber (FC3), through a firsttransfer conduit (KGD), second transfer conduit (KGE), third transferconduit (KGF), respectively. The first transfer conduit (KGD), secondtransfer conduit (KGE), and third transfer conduit (KGF) merge into onecommon header (KGF′) and are then connected to the large insectseparator (KGA). The large insect separator (KGA) separates largeinsects (KGG) from the large insect-small insect-particulate-gas mixture(KGJ). A small insect-particulate-gas mixture (KGK) is evacuated fromthe large insect separator (KGA) and sent to the small insect separator(KGB). The small insect separator (KGB) separates small insects (KGH)from the small insect-particulate-gas mixture (KGK) and transfers thesmall insects (KGH) back to the first feeding chamber (FC1), secondfeeding chamber (FC2), and third feeding chamber (FC3).

The small insect separator (KGB) separates small insects (KGH) from thesmall insect-particulate-gas mixture (KGK) and transfers the a firstsmall insect portion (KGR) back to the first feeding chamber (FC1) via afourth transfer conduit (KGO). The small insect separator (KGB)separates small insects (KGH) from the small insect-particulate-gasmixture (KGK) and transfers the second small insect portion (KGS) backto the second feeding chamber (FC2) via a fifth transfer conduit (KGP).The small insect separator (KGB) separates small insects (KGH) from thesmall insect-particulate-gas mixture (KGK) and transfers a third smallinsect portion (KGT) back to the third feeding chamber (FC3) via a fifthtransfer conduit (KGQ).

A particulate-gas mixture (KGL) is evacuated from the small insectseparator (KGB) and sent to the particulate separator (KGC). Theparticulate separator (KGC) separates particulates (KGI) from theparticulate-gas mixture (KGL). The particulates include chitin. A gas(KGM) is evacuated from the particulate separator (KGC) and is sentthrough a fan (KGM) and then into an odor control system (KGN). Inembodiments, the odor control system (KGN) includes an adsorbent,sorbent, or a filter.

FIG. 17:

FIG. 17 shows a perspective view of one embodiment of a scalableportable modular Insect Production Superstructure System (IPSS) designedwith: one enhanced feedstock mixing module (1000); three insect feedingmodules (2000A, 2000B, 2000C); one insect evacuation module (3000);three insect breeding modules (4000A, 4000B, 4000C), and three insectseparation modules (5000).

FIG. 17 shows a perspective view of one embodiment of a scalableportable modular Insect Production Superstructure System (IPSS) designedwith: one enhanced feedstock mixing module (1000); three insect feedingmodules (2000A, 2000B, 2000C); one insect evacuation module (3000);three insect breeding modules (4000A, 4000B, 4000C), and three insectseparation modules (5000).

In one embodiment, each module (1000, 2000A, 2000B, 2000C, 3000, 4000A,4000B, 4000C, 5000) container is a 40 feet high shipping containerconforming to the International Organization for Standardization (ISO)specifications. In another embodiment, the container may measure 40feet×8 feet×9.6 feet. In another embodiment, other containers ofdifferent sizes may be used.

In embodiments, each module (1000, 2000A, 2000B, 2000C, 3000, 4000A,4000B, 4000C, 5000) may be positioned on high density plastic ties(HDT). The high density plastic ties (HDT) provide stability to themodule (1000, 2000A, 2000B, 2000C, 3000, 4000A, 4000B, 4000C, 5000) ofthe Insect Production Superstructure System (IPSS) and may be cheaperand faster to install than traditional concrete foundations. In anotherembodiment, each of the module (1000, 2000A, 2000B, 2000C, 3000, 4000A,4000B, 4000C, 5000) may be positioned on concrete foundations.Electrical cables may be contained in a plurality of fiberglass cabletrays (FGT) placed between each module (1000, 2000A, 2000B, 2000C, 3000,4000A, 4000B, 4000C, 5000).

The embodiment of FIG. 17 shows the enhanced feedstock mixing module(1000) including a feedstock distribution module (1A), mineraldistribution module (1B), vitamin distribution module (1C), polymerdistribution module (1D), water distribution module (1E), and enhancedfeedstock distribution module (1F),

However, as depicted in FIGS. 18-20 the water distribution module (1E)and enhanced feedstock distribution module (1F) may be separate from theenhanced feedstock mixing module (1000). A separate water distributionmodule (1E) and a separate enhanced feedstock distribution module (1F)are not shown in FIG. 17 because it these modules (1E, 1F) are designedto be housed within the enhanced feedstock mixing module (1000). Aseparate water distribution module (1E) is shown in FIGS. 21-23. Aseparate and a separate enhanced feedstock distribution module (1F) isshown in FIGS. 24-26.

In the non-limiting example of FIG. 17 for a variable-scale, modular,easily manufacturable, energy efficient, reliable, and computer operatedInsect Production Superstructure Systems (IPSS) shows one enhancedfeedstock mixing module (1000) in fluid communication with a firstinsect feeding module (2000A), second insect feeding module (2000B), anda third insect feeding module (2000C).

A first enhanced feedstock stream (EF1) is configured to pass from theenhanced feedstock mixing module (1000) to the first insect feedingmodule (2000A). A second enhanced feedstock stream (EF2) is configuredto pass from the enhanced feedstock mixing module (1000) to the secondinsect feeding module (2000B). A third enhanced feedstock stream (EF3)is configured to pass from the enhanced feedstock mixing module (1000)to the third insect feeding module (2000C).

Each of the first insect feeding module (2000A), second insect feedingmodule (2000B), third insect feeding module (2000C), are connected toone common insect evacuation module (3000) via a common entry conduit(CEC). The common entry conduit (CEC) is connected at one end to theinsect evacuation module (3000) and connected at one end to the firstinsect feeding module (2000A) via a first feeding chamber insectevacuation output (205A). The common entry conduit (CEC) is connected atone end to the insect evacuation module (3000) and connected at one endto the second insect feeding module (2000B) via a second feeding chamberinsect evacuation output (205B). The common entry conduit (CEC) isconnected at one end to the insect evacuation module (3000) andconnected at one end to the third insect feeding module (2000C) via athird feeding chamber insect evacuation output (205C). Each insectfeeding module (2000A, 2000B, 2000C) is connected to its own insectbreeding module (4000A, 4000B, 4000C). The first insect feeding module(2000A) is connected to the first insect breeding module (4000A) via afeeding chamber 1 egg-laden breeding material transfer line (R1). Thesecond insect feeding module (2000B) is connected to the second insectbreeding module (4000B) via a feeding chamber 2 egg-laden breedingmaterial transfer line (R2). The third insect feeding module (2000C) isconnected to the third insect breeding module (4000C) via a feedingchamber 3 egg-laden breeding material transfer line (R3).

Each insect breeding module (4000A, 4000B, 4000C) is connected to itsown hatched insect separation module (5000A, 5000B, 5000C). The firstinsect breeding module (4000A) is connected to the first hatched insectseparation module (5000A) via a breeding chamber 1 hatched egg andbreeding material transfer line (U1). The second insect breeding module(4000B) is connected to the second hatched insect separation module(5000B) via a breeding chamber 2 hatched egg and breeding materialtransfer line (U2). The third insect breeding module (4000C) isconnected to the third hatched insect separation module (5000C) via abreeding chamber 3 hatched egg and breeding material transfer line (U3).

Each hatched insect separation module (5000A, 5000B, 5000C) is connectedto any of the plurality of insect feeding modules (2000A, 2000B, 2000C)via a first hatched insect output (DFC), second hatched insect output(EFC), and third hatched insect output (FFC). The first hatched insectoutput (DFC) of the first hatched insect separation module (5000A) is influid communication with the first insect feeding module (2000A) via afirst hatched insect input (AFC). The first hatched insect output (DFC)of the first hatched insect separation module (5000A) is in fluidcommunication with the second insect feeding module (2000B) via a secondhatched insect input (BFC). The first hatched insect output (DFC) of thefirst hatched insect separation module (5000A) is in fluid communicationwith the third insect feeding module (2000C) via a third hatched insectinput (CFC).

The second hatched insect output (EFC) of the second hatched insectseparation module (5000B) is in fluid communication with the firstinsect feeding module (2000A) via a first hatched insect input (AFC).The second hatched insect output (EFC) of the second hatched insectseparation module (5000B) is in fluid communication with the secondinsect feeding module (2000B) via a second hatched insect input (BFC).The second hatched insect output (EFC) of the second hatched insectseparation module (5000B) is in fluid communication with the thirdinsect feeding module (2000C) via a third hatched insect input (CFC).

The third hatched insect output (FFC) of the third hatched insectseparation module (5000C) is in fluid communication with the firstinsect feeding module (2000A) via a first hatched insect input (AFC).The third hatched insect output (FFC) of the third hatched insectseparation module (5000C) is in fluid communication with the secondinsect feeding module (2000B) via a second hatched insect input (BFC).The third hatched insect output (FFC) of the third hatched insectseparation module (5000C) is in fluid communication with the thirdinsect feeding module (2000C) via a third hatched insect input (CFC).

FIG. 18:

FIG. 18 shows a front view of one embodiment of an enhanced feedstockmixing module (1000) module including a feedstock distribution module(1A), mineral distribution module (1B), vitamin distribution module(1C), and a polymer distribution module (1D). The enhanced feedstockmixing module (1000) is shown to be contained within a 40 feet highshipping container conforming to the International Organization forStandardization (ISO) specifications.

The feedstock distribution module (1A) has feedstock (1A1) containedwithin the interior (1A3) of a feedstock tank (1A2). A feedstock masssensor (1A7) is provided to determine the loss in mass of the feedstocktank (1A2). The feedstock tank (1A2) has a live floor screw (1A21) witha motor (1A22) is configured to transfer feedstock (1A1) from theinterior (1A3) of the feedstock tank (1A2) to a feedstock conveyor (1A5)and an enhanced feedstock transport screw (1A20). A supply access door(1A15) is positioned above the feedstock input (1A4) and configured totransfer feedstock (1A1) to the interior (1A3) of the feedstock tank(1A2). A supply access door opening/closing unit (1A16) is operativelycoupled to the supply access door (1A15) and a weather seal (1A17) is incontact with the supply access door (1A15) to prevent rain and otherelements from entering the enhanced feedstock mixing module (1000).

The mineral distribution module (1B) has minerals (1B1) contained withinthe interior (1B3) of a mineral tank (1B2). A mineral mass sensor (1B7)is provided to determine the loss in mass of the mineral tank (1B2). Themineral tank (1B2) has a live floor screw (1B20) with a motor (1B21) isconfigured to transfer minerals (1B1) from the interior (1B3) of themineral tank (1B2) to a mineral conveyor (1B5) and an enhanced feedstocktransport screw (1A20) via an enhanced feedstock transport screwconnection (1B18). A supply access door (1B13) is positioned above themineral input (1B4) and configured to transfer minerals (1B1) to theinterior (1B3) of the mineral tank (1B2). A supply access dooropening/closing unit (1B14) is operatively coupled to the supply accessdoor (1B13) and a weather seal (1B15) is in contact with the supplyaccess door (1B13) to prevent rain and other elements from entering theenhanced feedstock mixing module (1000).

The vitamin distribution module (1C) has vitamins (1C1) contained withinthe interior (1C3) of a vitamin tank (1C2). A vitamin mass sensor (1C7)is provided to determine the loss in mass of the vitamin tank (1C2). Thevitamin tank (1C2) has a live floor screw (1C20) with a motor (1C21) isconfigured to transfer vitamins (1C1) from the interior (1C3) of thevitamin tank (1C2) to a vitamin conveyor (105) and an enhanced feedstocktransport screw (1A20) via an enhanced feedstock transport screwconnection (1C18). A supply access door (1C13) is positioned above thevitamin input (1C4) and configured to transfer vitamins (1C1) to theinterior (1C3) of the vitamin tank (1C2). A supply access dooropening/closing unit (1C14) is operatively coupled to the supply accessdoor (1C13) and a weather seal (1C15) is in contact with the supplyaccess door (1C13) to prevent rain and other elements from entering theenhanced feedstock mixing module (1000).

The polymer distribution module (1D). includes polymer (1D1) containedwithin the interior (1D3) of a polymer tank (1D2). A polymer mass sensor(1D7) is provided to determine the loss in mass of the polymer tank(1D2). The polymer tank (1D2) has a live floor screw (1D20) with a motor(1D21) is configured to transfer polymer (1D1) from the interior (1D3)of the polymer tank (1D2) to a polymer conveyor (1D5) and an enhancedfeedstock transport screw (1A20) via an enhanced feedstock transportscrew connection (1D18). A supply access door (1D13) is positioned abovethe polymer input (1D4) and configured to transfer polymer (1D1) to theinterior (1D3) of the polymer tank (1D2). A supply access dooropening/closing unit (1C14) is operatively coupled to the supply accessdoor (1C13) and a weather seal (1C15) is in contact with the supplyaccess door (1C13) to prevent rain and other elements from entering theenhanced feedstock mixing module (1000).

A dry enhanced feedstock (DEF) is outputted from the enhanced feedstockmixing module (1000) via the enhanced feedstock transport screw (1A20).A feedstock moisture sensor (1A12A) is interposed on the enhancedfeedstock transport screw (1A20) to measure the water content of the dryenhanced feedstock (DEF). Alternately, the feedstock moisture sensor(1A12A) may be positioned on the enhanced feedstock transport screw(1A20) after the minerals (1B1), vitamins (1C1), polymer (1D1) have beenmixed with the feedstock (1A1). The enhanced feedstock mixing module(1000) may be equipped with a low voltage disconnect switch (1000LV) anda computer (COMP).

FIG. 19:

FIG. 19 shows a top view of one embodiment of an enhanced feedstockmixing module (1000) including a feedstock distribution module (1A),mineral distribution module (1B), vitamin distribution module (1C), anda polymer distribution module (1D).

Feedstock (1A1) within the feedstock tank (1A2), minerals (1B1) withinthe mineral tank (1B2), vitamins (1C1) within the vitamin tank (1C2),and polymer (1D1) within the polymer tank (1D2) are all mixed togetherin an enhanced feedstock transport screw (1A20). A live floor screw(1A21) equipped with a motor (1A22) is positioned within the feedstocktank (1A2). The live floor screw (1A21) transfers feedstock (1A1) to afeedstock conveyor (1A5). The feedstock conveyor (1A5) has a feedstockconveyor output (1A6) that is connected to a feedstock transfer line(1A14). The feedstock transfer line (1A14) is connected at one end tothe feedstock conveyor output (1A6) and at another end to the enhancedfeedstock transport screw (1A20) via an enhanced feedstock transportscrew connection (1A20A). The feedstock distribution module (1A) isequipped with an air inlet vent (1A18) that is configured to input air(1A19) to the feedstock distribution module (1A) portion of the enhancedfeedstock mixing module (1000). A feedstock module access door (1A23) isprovided to access the feedstock distribution module (1A) portion of theenhanced feedstock mixing module (1000).

A live floor screw (1B20) equipped with a motor (1B21) is positionedwithin the mineral tank (1B2). The live floor screw (1B20) transfersminerals (1B1) to a mineral conveyor (1B5). The mineral conveyor (1B5)has a mineral conveyor output (1B6) that is connected to a mineraltransfer line (1B12). The mineral transfer line (1B12) is connected atone end to the mineral conveyor output (1B6) and at another end to theenhanced feedstock transport screw (1A20) via an enhanced feedstocktransport screw connection (1B18). The mineral distribution module (1B)is equipped with an air inlet vent (1B16) that is configured to inputair (1B17) to the mineral distribution module (1B) portion of theenhanced feedstock mixing module (1000). A mineral module access door(1B22) is provided to access the mineral distribution module (1B)portion of the enhanced feedstock mixing module (1000).

A live floor screw (1C20) equipped with a motor (1C21) is positionedwithin the vitamin tank (1D2). The live floor screw (1C20) transfersvitamins (1C1) to a vitamin conveyor (105). The vitamin conveyor (105)has a vitamin conveyor output (106) that is connected to a vitamintransfer line (1C12). The vitamin transfer line (1C12) is connected atone end to the vitamin conveyor output (106) and at another end to theenhanced feedstock transport screw (1A20) via an enhanced feedstocktransport screw connection (1C18). The vitamin distribution module (1C)is equipped with an air inlet vent (1C16) that is configured to inputair (1C17) to the vitamin distribution module (1C) portion of theenhanced feedstock mixing module (1000). A vitamin module access door(1C22) is provided to access the vitamin distribution module (1C)portion of the enhanced feedstock mixing module (1000).

A live floor screw (1D20) equipped with a motor (1D21) is positionedwithin the polymer tank (1D2) to transfer polymer (1D1) to a polymerconveyor (1D5). The polymer conveyor (1D5) has a polymer conveyor output(1D6) that is connected to a polymer transfer line (1D12). The polymertransfer line (1D12) is connected at one end to the polymer conveyoroutput (1D6) and at another end to the enhanced feedstock transportscrew (1A20) via an enhanced feedstock transport screw connection(1D18). The polymer distribution module (1D) is equipped with an airinlet vent (1D16) that is configured to input air (1D17) to the polymerdistribution module (1D) portion of the enhanced feedstock mixing module(1000). A polymer module access door (1D22) is provided to access thepolymer distribution module (1D) portion of the enhanced feedstockmixing module (1000). The polymer distribution module (1D) is in fluidcommunication with the third separator (S3) particulate separator (S3A)of the insect evacuation module (3000). The polymer tank (1D2) isconfigured to accept a polymer (1D1) from a portion of the separatedparticulate stream (370) of the separated insect conveyor (328) of thethird separator (S3) particulate separator (S3A).

FIG. 20:

FIG. 20 shows a first side view of one embodiment of an enhancedfeedstock mixing module (1000). Visible from the first side view of theenhanced feedstock mixing module (1000) is the supply access door (1A15)that is opened and closed by a supply access door opening/closing unit(1A16) wherein a weather seal (1A17) prevents rain and other elementsfrom entering the enhanced feedstock mixing module (1000).

Feedstock (1A1) is contained within the interior (1A3) of the feedstocktank (1A2). Feedstock (1A1) is added to the enhanced feedstock mixingmodule (1000) through the supply access door (1A15) where it enters thefeedstock input (1A4) and into the interior (1A3) of the feedstock tank(1A2). A live floor screw (1A21) is positioned in the interior (1A3) ofthe feedstock tank (1A2). The live floor screw (1A21) is configured totransfer feedstock (1A1) from the interior (1A3) of the feedstock tank(1A2) into a feedstock conveyor (1A5). The feedstock conveyor motor(1A9) drives the feedstock conveyor (1A5) to transport feedstock (1A1)through the feedstock conveyor output (1A6) and into the enhancedfeedstock transport screw (1A20) via an enhanced feedstock transportscrew connection (1A20A). A feedstock mass sensor (1A7) may bepositioned on the feedstock conveyor (1A5) to measure the mass loss andcontrol to a pre-determined feedstock mass flow rate into the enhancedfeedstock transport screw (1A20). Also visible is the feedstock moduleaccess door (1A23) and an air inlet vent (1A18) which permits air (1A19)to enter the feedstock distribution module (1A) portion of the enhancedfeedstock mixing module (1000).

FIG. 21:

FIG. 21 shows a front view of one embodiment of a water distributionmodule (1E). The following description for FIG. 21 also applies to FIG.22 since the reference numerals for FIG. 20 and FIG. 21 are identical.The water distribution module (1E) is shown to be contained within a 40feet high shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

The water distribution module (1E) contains a first water treatment unit(1E6), second water treatment unit (1E11), water distribution module(1E) enhancer tank (1E45) and a water supply pump (1E22). A water inputline (1E4) enters the water distribution module (1E) and is connected tothe first water treatment unit (1E6) at a first water treatment unitinput (1E7). A first water pressure sensor (1E2) is installed on thewater input line (1E4). The first water treatment unit (1E6) may containa contain an adsorbent, ion-exchange resin, catalyst, or activatedcarbon.

The first water treatment unit (1E6) is connected to the second watertreatment unit (1E11) via a first contaminant-depleted water transferline (1E10). The first contaminant-depleted water transfer line (1E10)is connected at one end to the first water treatment unit output (1E8)of the first water treatment unit (1E6) and connected at a second end tothe second water treatment unit input (1E12) of the second watertreatment unit (1E11). The second water treatment unit (1E11) maycontain a contain an adsorbent, ion-exchange resin, catalyst, oractivated carbon. The system as shown in FIGS. 21-23 may, for example beused to decontaminate water that contains positively charged ions andnegatively charged ions and optionally undesirable compounds. Thepositively charged ions are comprised of one or more from the groupconsisting of calcium, magnesium, sodium, and iron. The negativelycharged ions are comprised of one or more from the group consisting ofiodine, chloride, and sulfate. The undesirable compounds are comprisedof one or more from the group consisting of dissolved organic chemicals,viruses, bacteria, and particulates. In embodiments, the first watertreatment unit (1E6) contains activated carbon and the second watertreatment unit (1E11) contains a molecular sieve adsorbent. Inembodiments, the positively charged ions are comprised of one or morefrom the group consisting of calcium, magnesium, sodium, and iron. Inembodiments, the positively charged ions are comprised of one or morefrom the group consisting of aluminum, barium, beryllium, calcium,chromium(III), copper(I), copper(II), hydrogen, iron(II), iron(III),lead(II), lead(IV), lithium, magnesium, manganese(II), mercury(II),potassium, silver, sodium, strontium, tin(II), tin(IV), and zinc. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of iodine, chloride, and sulfate. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of acetate, aluminum silicate, anions fromorganic acids, azide, bromide, carbonate, chlorate, chloride, chromate,cyanide, dichromate, dihydrogen phosphate, fluoride, formate, hydride,hydrogen carbonate, hydrogen sulfate, hydrogen sulfite, hydroxide,hypochlorite, iodide, metasilicate, monohydrogen phosphate, nitrate,nitride, nitrite, oxalate, oxide, perchlorate, permanganate, peroxide,phosphate, silicate, sulfate, sulfide, sulfite, superoxide, andthiosulfate.

In embodiments, the first water treatment unit (1E6) includes a cationconfigured to remove positively charged ions from water to form apositively charged ion depleted water, the positively charged ions arecomprised of one or more from the group consisting of calcium,magnesium, sodium, and iron. In embodiments, the second water treatmentunit (1E11) includes an anion configured to remove negatively chargedions from the positively charged ion depleted water to form a negativelycharged ion depleted water, the negatively charged ions are comprised ofone or more from the group consisting of iodine, chloride, and sulfate.

In embodiments, the positively charged ions are comprised of one or morefrom the group consisting of calcium, magnesium, sodium, and iron. Inembodiments, the positively charged ions are comprised of one or morefrom the group consisting of aluminum, barium, beryllium, calcium,chromium(III), copper(I), copper(II), hydrogen, iron(II), iron(III),lead(II), lead(IV), lithium, magnesium, manganese(II), mercury(II),potassium, silver, sodium, strontium, tin(II), tin(IV), and zinc. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of iodine, chloride, and sulfate. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of acetate, aluminum silicate, anions fromorganic acids, azide, bromide, carbonate, chlorate, chloride, chromate,cyanide, dichromate, dihydrogen phosphate, fluoride, formate, hydride,hydrogen carbonate, hydrogen sulfate, hydrogen sulfite, hydroxide,hypochlorite, iodide, metasilicate, monohydrogen phosphate, nitrate,nitride, nitrite, oxalate, oxide, perchlorate, permanganate, peroxide,phosphate, silicate, sulfate, sulfide, sulfite, superoxide, andthiosulfate.

In embodiments, the first water treatment unit (1E6) includes a cationand an anion. In embodiments, the second water treatment unit (1E11)includes a membrane configured to remove undesirable compounds from thenegatively charged ion depleted water to form an undesirable compoundsdepleted water, the undesirable compounds are comprised of one or morefrom the group consisting of dissolved organic chemicals, viruses,bacteria, and particulates. In embodiments, the second water treatmentunit (1E11) includes a membrane configured to remove undesirablecompounds from the water to form an undesirable compounds depletedwater, the undesirable compounds are comprised of one or more from thegroup consisting of dissolved organic chemicals, viruses, bacteria, andparticulates.

The second water treatment unit (1E11) is connected to the water tank(1E16) via a second contaminant-depleted water transfer line (1E15). Thesecond contaminant-depleted water transfer line (1E15) is connected atone end to the second water treatment unit output (1E13) of the secondwater treatment unit (1E11) and connected at another end to the waterinput (1E18) of the water tank (1E16). A water supply valve (1E23) witha controller (1E24) is interposed on the second contaminant-depletedwater transfer line (1E15) in between the second water treatment unit(1E11) and water tank (1E16). The water tank (1E16) has an interior(1E17) that contains water (1E1). The water tank (1E16) is equipped witha high water level sensor (1E26) and a low water level sensor (1E28).

Enhancers (1E44) contained within the interior (1E46) of the enhancertank (1E45) may be routed to the interior (1E17) of the water tank(1E16) through an enhancer transfer line (1E48). The enhancer transferline (1E48) is connected at one end to the enhancer tank output (1E47)of the enhancer tank (1E45) and connected at another end to the enhancerinput (1E49) of the water tank (1E16). A water enhancer supply valve(1E52) with a controller (1E53) is interposed on the enhancer transferline (1E48) in between the enhancer tank (1E45) and the water tank(1E16). An enhancer flow sensor (1E50) is interposed on the enhancertransfer line (1E48) in between the enhancer tank (1E45) and the watertank (1E16).

A water supply pump (1E22) is connected to the water tank (1E16) via awater discharge line (1E21). The water supply pump (1E22) is configuredto remove water (1E1), and enhancers (1E44), from the interior (1E17) ofthe water tank (1E16) for transfer downstream to be mixed with a dryenhanced feedstock (DEF) to create a wet enhanced feedstock (WEF). Thewater discharge line (1E21) is connected at one end to the water output(1E20) of the water tank (1E16) and connected at another end to thewater supply pump (1E22).

The water supply pump (1E22) pulls a suction on the water discharge line(1E21) of the water tank (1E16) and increases the pressure of the (1E1)and outputs pressurized water via a water transfer line (1E41). Thewater transfer line (1E41) has a variety of instrumentation installed onit, including: a water flow sensor (1E34); a water control valve (1E36);a third water pressure sensor (1E39); and, a water quality sensor(1E42). A second water pressure sensor (1E30) is installed on the watertransfer line (1E41) upstream of the water control valve (1E36) andcloser to the water supply pump (1E22). In embodiments, the pressuredrop across the water control valve (1E36) may range from: between about1 pound per square inch to about 5 pound per square inch; between about5 pound per square inch to about 10 pound per square inch; between about10 pound per square inch to about 15 pound per square inch; betweenabout 15 pound per square inch to about 20 pound per square inch;between about 25 pound per square inch to about 30 pound per squareinch; between about 35 pound per square inch to about 40 pound persquare inch; between about 45 pound per square inch to about 50 poundper square inch; between about 55 pound per square inch to about 60pound per square inch; between about 65 pound per square inch to about70 pound per square inch; between about 75 pound per square inch toabout 80 pound per square inch; between about 85 pound per square inchto about 90 pound per square inch; between about 95 pound per squareinch to about 100 pound per square inch; between about 100 pound persquare inch to about 125 pound per square inch; between about 125 poundper square inch to about 150 pound per square inch; or, between about150 pound per square inch to about 200 pound per square inch.

The water transfer line (1E41) is discharged from the water distributionmodule (1E) en route to the enhanced feedstock distribution module (1F)on FIGS. 24-26. The water distribution module (1E) contains a firstaccess door (1E55) at one end and a second access door (1E56) at anotherend. The water distribution module (1E) also contains an air vent (1E57)for introduction of an air supply (1E58). The water distribution module(1E) also contains a low voltage disconnect switch (1E59) and a computer(COMP)

FIG. 22:

FIG. 22 shows a top view of one embodiment of a water distributionmodule (1E). Refer to the text in the preceding section for thedescription of FIG. 22.

FIG. 23:

FIG. 23 shows a first side view of one embodiment of a waterdistribution module (1E). Visible from the first side view of the waterdistribution module (1E) is the first access door (1E55) along with theair vent (1E57) for introduced on an air supply (1E58). A water inputline (1E4) containing is shown entering the first water treatment unit(1E6) via a first water treatment unit input (1E7). Water (1E1) is showncontained within the interior (1E17) of the water tank (1E16). Enhancers(1E44) are shown contained within the interior (1E46) of the enhancertank (1E45).

FIG. 24:

FIG. 24 shows a front view of one embodiment of an enhanced feedstockdistribution module (1F). The enhanced feedstock distribution module(1F) is shown to be contained within a 40 feet high shipping containerconforming to the International Organization for Standardization (ISO)specifications. Water (1E1) enters from the left-hand-side of theenhanced feedstock distribution module (1F) via a water transfer line(1E41). The water (1E1) is mixed with a dry enhanced feedstock (DEF) toform a wet enhanced feedstock (WEF). The dry enhanced feedstock (DEF)enters from the left-hand-side of the enhanced feedstock distributionmodule (1F) via an enhanced feedstock transport screw (1A20). A wetenhanced feedstock (WEF) is transported to the enhanced feedstocksplitter (1F1) via an enhanced feedstock transfer line (1F0). Anenhanced feedstock moisture sensor (1A12B) is installed on the enhancedfeedstock transfer line (1F0). In embodiments, the wet enhancedfeedstock (WEF) may be introduced to the enhanced feedstock splitter(1F1) through an enhanced feedstock transfer line (1F0) via a pluralityof inputs (1F3A, 1F3B, 1F3C). Each of the first splitter input (1F3A),second splitter input (1F3B), and third splitter input (1F3C), transfera wet enhanced feedstock (WEF) to the interior (1F2) of the enhancedfeedstock splitter (1F1).

The enhanced feedstock splitter (1F1) has a top section (1F4), bottomsection (1F5), and an interior (1F2) defined by at least one side wall(1F6). A first splitter level sensor (1F7) is positioned on the sidewall (1F6). The enhanced feedstock splitter (1F1) is shown equipped witha splitter first screw conveyor (1F9) and a splitter second screwconveyor (1F14) both positioned at the bottom section (1F5) of theenhanced feedstock splitter (1F1). The splitter first screw conveyor(1F9) transfers enhanced feedstock from the interior (1F2) of theenhanced feedstock splitter (1F1) to a first weigh screw (1F24) via afirst output (1F10). The splitter second screw conveyor (1F14) transfersenhanced feedstock from the interior (1F2) of the enhanced feedstocksplitter (1F1) to a second weigh screw (1F33) via a second output(1F15). The enhanced feedstock distribution module (1F) is shownequipped with a low voltage disconnect switch (1F55) and a computer(COMP).

FIG. 25:

FIG. 25 shows a top view of one embodiment of an enhanced feedstockdistribution module (1F). The enhanced feedstock distribution module(1F) is shown to be contained within a 40 feet high shipping containerconforming to the International Organization for Standardization (ISO)specifications. Water (1E1) enters from the left-hand-side of theenhanced feedstock distribution module (1F) via a water transfer line(1E41). The water (1E1) is mixed with a dry enhanced feedstock (DEF) toform a wet enhanced feedstock (WEF). The dry enhanced feedstock (DEF)enters from the left-hand-side of the enhanced feedstock distributionmodule (1F) via an enhanced feedstock transport screw (1A20). A wetenhanced feedstock (WEF) is transported to the enhanced feedstocksplitter (1F1) via an enhanced feedstock transfer line (1F0). Anenhanced feedstock moisture sensor (1A12B) is installed on the enhancedfeedstock transfer line (1F0). In embodiments, the wet enhancedfeedstock (WEF) may be introduced to the enhanced feedstock splitter(1F1) through an enhanced feedstock transfer line (1F0) via a pluralityof inputs (1F3A, 1F3B, 1F3C). Each of the first splitter input (1F3A),second splitter input (1F3B), and third splitter input (1F3C), transfera wet enhanced feedstock (WEF) to the interior (1F2) of the enhancedfeedstock splitter (1F1).

The enhanced feedstock splitter (1F1) has an interior (1F2) defined byat least one side wall (1F6). A first splitter level sensor (1F7) ispositioned on the side wall (1F6). The enhanced feedstock splitter (1F1)is shown equipped with a splitter first screw conveyor (1F9) and asplitter second screw conveyor (1F14) both positioned within theinterior (1F2) of the enhanced feedstock splitter (1F 1).

The splitter first screw conveyor (1F9) transfers enhanced feedstockfrom the interior (1F2) of the enhanced feedstock splitter (1F1) to afirst weigh screw (1F24) via a first output (1F10). The first weighscrew (1F24) has a first weigh screw input (1F25) and a first weighscrew output (1F26). The first weigh screw input (1F25) of the firstweigh screw (1F24) accepts enhanced feedstock from the first output(1F10) of the splitter first screw conveyor (1F9). The splitter firstscrew conveyor (1F9) is equipped with a splitter first screw conveyormotor (1F11). The first weigh screw (1F24) is configured to discharge afirst weighed enhanced feedstock stream (1F32) or a first enhancedfeedstock stream (EF1) via the first weigh screw output (1F26). Thefirst weighed enhanced feedstock stream (1F32) or the first enhancedfeedstock stream (EF1) is discharged from the first weigh screw output(1F26) where it is then transferred to a first feeding chamber (FC1).The first weigh screw (1F24) is equipped with a mass sensor (1F27) and afirst weigh screw motor (1F29).

The splitter second screw conveyor (1F14) transfers enhanced feedstockfrom the interior (1F2) of the enhanced feedstock splitter (1F1) to asecond weigh screw (1F33) via a second output (1F15). The second weighscrew (1F33) has a second weigh screw input (1F34) and a second weighscrew output (1F35). The second weigh screw input (1F34) of the secondweigh screw (1F33) accepts enhanced feedstock from the second output(1F15) of the splitter second screw conveyor (1F14). The splitter secondscrew conveyor (1F14) is equipped with a splitter second screw conveyormotor (1F16). The second weigh screw (1F33) is configured to discharge asecond weighed enhanced feedstock stream (1F41) or a second enhancedfeedstock stream (EF2) via the second weigh screw output (1F35). Thesecond weighed enhanced feedstock stream (1F41) or the second enhancedfeedstock stream (EF2) is discharged from the second weigh screw output(1F35) where it is then transferred to a second feeding chamber (FC2).The second weigh screw (1F33) is equipped with a mass sensor (1F36) anda second weigh screw motor (1F38).

The enhanced feedstock distribution module (1F) is shown equipped with alow voltage disconnect switch (1F55) and a computer (COMP). Also shownis a first access door (1F51), second access door (1F52), and an airvent (1F53) configured to introduce an air supply (1F54) to the enhancedfeedstock distribution module (1F).

FIG. 26:

FIG. 26 shows a first side view of one embodiment of an enhancedfeedstock distribution module (1F). Visible from the first side view ofthe enhanced feedstock transfer line (1F0) is the first access door(1F51) along with the air vent (1F53) for introduced on an air supply(1F54). The enhanced feedstock splitter (1F1) is shown to have aninterior (1F2) defined by at least one side wall (1F6). A first splitterlevel sensor (1F7) is positioned on the side wall (1F6). The enhancedfeedstock splitter (1F1) has a top section (1F4) and a bottom section(1F5). A splitter second screw conveyor (1F14) is positioned within theinterior (1F2) of the enhanced feedstock splitter (1F1) at the bottomsection (1F5).

A water transfer line (1E41) is shown entering the enhanced feedstocktransfer line (1F0) where it mixes with enhanced feedstock and is routedto the interior (1F2) of the enhanced feedstock splitter (1F1) via anenhanced feedstock transfer line (1F0) and a first splitter input(1F3A). The first splitter input (1F3A) has an insertion distance(1F3A1) positioned within the interior (1F2) of the enhanced feedstocksplitter (1F1). In embodiments, the insertion distance (1F3A1) may rangefrom: between about 2 inches to about 4 inches; between about 4 inchesto about 8 inches; between about 8 inches to about 12 inches; betweenabout 12 inches to about 16 inches; between about 16 inches to about 20inches; between about 20 inches to about 24 inches; between about 24inches to about 28 inches; between about 28 inches to about 30 inches;between about 30 inches to about 34 inches; between about 34 inches toabout 36 inches; between about 36 inches to about 40 inches; betweenabout 40 inches to about 44 inches; between about 44 inches to about 46inches; between about 46 inches to about 50 inches; or, between about 50inches to about 60 inches.

A second output (1F15) is shown at the bottom section (1F5) of theenhanced feedstock splitter (1F1). A second weigh screw (1F33) is shownto have a second weigh screw input (1F34) and a second weigh screwoutput (1F35). The second weigh screw input (1F34) is connected to thesecond output (1F15) is shown at the bottom section (1F5) of theenhanced feedstock splitter (1F1). The second weigh screw (1F33) isequipped with a mass sensor (1F36) and a second weigh screw motor(1F38). The second weighed enhanced feedstock stream (1F41) or thesecond enhanced feedstock stream (EF2) is discharged from the secondweigh screw output (1F35) where it is then transferred to a secondfeeding chamber (FC2).

FIG. 27A:

FIG. 27A shows a front view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C). Referring to FIGS. 27-29, the insectfeeding module (2000, 2000A, 2000B, 2000C) is shown to be containedwithin a 40 feet high shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 27A shows an insect feeding module (2000, 2000A, 2000B, 2000C)containing a network (220) of cells (219) for growing insects (225). Thenetwork (220) of cells (219) has openings (222) first end (221) andopenings (224) of the second end (223). A vibration unit (214) equippedwith a vibration unit motor (215) is operatively connected to thenetwork (220) of cells (219) via a first vibration unit connection(218A) and a second vibration unit connection (218B). The vibration unit(214) is configured to vibrate at least a portion of the network (220)of cells (219) to assist in removal of insects (225) contained therein.

In embodiments, the network (220) of cells (219) has a network length(N-L) that is greater than the network width (N-W). In embodiments, thenetwork (220) of cells (219) has a network length (N-L) that is lessthan the network width (N-W). In one example, as in the non-limitingembodiments of FIGS. 27-29, the network width (N-W) is approximatelyabout between about 4 feet to about 5 feet, and the network length (N-L)is approximately about between about 30 feet to about 31 feet to fitwithin the shipping container and allowing for access and maintenance.

In embodiments, the network length (N-L) ranges from: 0.5 feet to about1 foot; between about 1 feet to about 2 feet; between about 2 feet toabout 3 feet; between about 3 feet to about 4 feet; between about 4 feetto about 5 feet; between about 5 feet to about 6 feet; between about 6feet to about 7 feet; between about 7 feet to about 8 feet; betweenabout 8 feet to about 9 feet; between about 9 feet to about 10 feet;between about 10 feet to about 11 feet; between about 11 feet to about12 feet; between about 12 feet to about 13 feet; between about 13 feetto about 14 feet; between about 14 feet to about 15 feet; between about15 feet to about 16 feet; between about 16 feet to about 17 feet;between about 17 feet to about 18 feet; between about 18 feet to about19 feet; between about 19 feet to about 20 feet; between about 20 feetto about 21 feet; between about 21 feet to about 22 feet; between about22 feet to about 23 feet; between about 23 feet to about 24 feet;between about 24 feet to about 25 feet; between about 25 feet to about26 feet; between about 26 feet to about 27 feet; between about 27 feetto about 28 feet; between about 28 feet to about 29 feet; between about29 feet to about 30 feet; between about 30 feet to about 31 feet;between about 31 feet to about 32 feet; between about 32 feet to about33 feet; between about 33 feet to about 34 feet; between about 34 feetto about 35 feet; between about 35 feet to about 36 feet; between about36 feet to about 37 feet; between about 37 feet to about 38 feet;between about 38 feet to about 39 feet; and, between about 39 feet toabout 40 feet.

In embodiments, the network width (N-W) ranges from: 0.5 feet to about 1foot; between about 1 feet to about 2 feet; between about 2 feet toabout 3 feet; between about 3 feet to about 4 feet; between about 4 feetto about 5 feet; between about 5 feet to about 6 feet; between about 6feet to about 7 feet; between about 7 feet to about 8 feet; betweenabout 8 feet to about 9 feet; between about 9 feet to about 10 feet;between about 10 feet to about 11 feet; between about 11 feet to about12 feet; between about 12 feet to about 13 feet; between about 13 feetto about 14 feet; between about 14 feet to about 15 feet; between about15 feet to about 16 feet; between about 16 feet to about 17 feet;between about 17 feet to about 18 feet; between about 18 feet to about19 feet; between about 19 feet to about 20 feet; between about 20 feetto about 21 feet; between about 21 feet to about 22 feet; between about22 feet to about 23 feet; between about 23 feet to about 24 feet;between about 24 feet to about 25 feet; between about 25 feet to about26 feet; between about 26 feet to about 27 feet; between about 27 feetto about 28 feet; between about 28 feet to about 29 feet; between about29 feet to about 30 feet; between about 30 feet to about 31 feet;between about 31 feet to about 32 feet; between about 32 feet to about33 feet; between about 33 feet to about 34 feet; between about 34 feetto about 35 feet; between about 35 feet to about 36 feet; between about36 feet to about 37 feet; between about 37 feet to about 38 feet;between about 38 feet to about 39 feet; and, between about 39 feet toabout 40 feet.

In embodiments, the interior (201) of the shipping container is theinterior (201) of the feeding chamber (200). The first side wall (202A)of the feeding chamber (200) is shown spaced apart from the firstshipping container side wall (CW-A). The second side wall (202B) of thefeeding chamber (200) is shown spaced apart from the second shippingcontainer side wall (CW-B). The third side wall (202C) of the feedingchamber (200) is shown spaced apart from the third shipping containerside wall (CW-C). The fourth side wall (202D) of the feeding chamber(200) is shown spaced apart from the fourth shipping container side wall(CW-D).

The top (203) of the feeding chamber (200) is shown to be the shippingcontainer top wall (CW-T). The first side wall (202A), second side wall(202B), third side wall (202C), fourth side wall (202D), may beflexible, perforated, wire or screen, or the like which is positionedextending into the interior (201) of the feeding chamber (200) from theat a side wall length (SW-L). No screen floor (258) is shown in FIGS.27-29 instead the bottom (204) of the feeding chamber (200) is open tothe surface of the conveyor (255) of the egg transfer system (244).

The first side wall (202A), second side wall (202B), third side wall(202C), and fourth side wall (202D) are spaced apart from the shippingcontainer side walls (CW-A, CW—B, CW-C, CW-D) so that the entireinterior (201) of the feeding chamber (200) is positioned directly abovethe conveyor (245) of the egg transfer system (244). This will allow forcomplete removal of all the contents from within the interior (201) ofthe feeding chamber (200) with the use of vibration or a vacuum or bothor none. In embodiments, when the first conveyor elevation unit (254)and second conveyor elevation unit (256) are extended at a secondelevated height (H2) there is no gap between the terminal end of theside wall length (SW-L) of each of the first side wall (202A), secondside wall (202B), third side wall (202C), and fourth side wall (202D).In embodiments, when the first conveyor elevation unit (254) and secondconveyor elevation unit (256) are extended at a second elevated height(H2) there is a gap between the terminal end of the second side walllength (202BL) only.

In embodiments, when the first conveyor elevation unit (254) and secondconveyor elevation unit (256) are extended at a second elevated height(H2) there is a gap between the terminal end of the first side walllength (202AL) and second side wall length (202BL). FIGS. 27-29 shownon-limiting embodiments of the insect feeding module (2000, 2000A,2000B, 2000C) contained within a shipping container and forrepresentative and illustrative purposes only show the first conveyorelevation unit (254) and second conveyor elevation unit (256) at a firstretracted height (H1). Refer to above text for modes of operation anddetailed description on the feeding chamber (200) integrated with theegg transfer system (244).

A first weighed enhanced feedstock stream (1F32) or synonymously termedfirst enhanced feedstock stream (EF1) enters the insect feeding module(2000, 2000A) on the left-hand-side through an enhanced feedstock input(206). The enhanced feedstock input (206) transfers a wet enhancedfeedstock (WEF) onto the conveyor (245) of the egg transfer system (244)through a plurality of enhanced feedstock inputs (206A, 206B, 206C) soas to be configured to evenly distribute the enhanced feedstock on theconveyor (245). In embodiments, the third side wall length (202CL) andfourth side wall length (202DL) are longer than the first side walllength (202AL) and second side wall length (202BL) so as to leave a gapin between the conveyor (245) and the terminal end of the first sidewall length (202AL) and second side wall length (202BL). In embodiments,the first side wall length (202AL), second side wall length (202BL),third side wall length (202CL), fourth side wall length (202DL), rangein between about 5 feet to about 6 feet so they may fit within theshipping container for interaction with the conveyor (245) of the eggtransfer system (244).

In embodiments, the first side wall length (202AL), second side walllength (202BL), third side wall length (202CL), fourth side wall length(202DL), range from: 0.5 feet to about 1 foot; between about 1 feet toabout 2 feet; between about 2 feet to about 3 feet; between about 3 feetto about 4 feet; between about 4 feet to about 5 feet; between about 5feet to about 6 feet; between about 6 feet to about 7 feet; betweenabout 7 feet to about 8 feet; between about 8 feet to about 9 feet;between about 9 feet to about 10 feet; between about 10 feet to about 11feet; between about 11 feet to about 12 feet; between about 12 feet toabout 13 feet; between about 13 feet to about 14 feet; between about 14feet to about 15 feet; between about 15 feet to about 16 feet; betweenabout 16 feet to about 17 feet; between about 17 feet to about 18 feet;between about 18 feet to about 19 feet; between about 19 feet to about20 feet; between about 20 feet to about 21 feet; between about 21 feetto about 22 feet; between about 22 feet to about 23 feet; between about23 feet to about 24 feet; between about 24 feet to about 25 feet;between about 25 feet to about 26 feet; between about 26 feet to about27 feet; between about 27 feet to about 28 feet; between about 28 feetto about 29 feet; between about 29 feet to about 30 feet; between about30 feet to about 31 feet; between about 31 feet to about 32 feet;between about 32 feet to about 33 feet; between about 33 feet to about34 feet; between about 34 feet to about 35 feet; between about 35 feetto about 36 feet; between about 36 feet to about 37 feet; between about37 feet to about 38 feet; between about 38 feet to about 39 feet; and,between about 39 feet to about 40 feet.

In embodiments, the first side wall (202A), second side wall (202B),third side wall (202C), and fourth side wall (202D) are made up of wire,screen, or mesh that is perforated with openings smaller than theaverage insect length (Ni-L) average insect width (Ni-W). Inembodiments, the first side wall (202A), second side wall (202B), thirdside wall (202C), and fourth side wall (202D) are made up of a plastic,rubber, or an impermeable substance, such as a tarp, curtain, cloth, orsheet and does not have openings in it.

An egg-depleted breeding material (246) enters the insect feeding module(2000, 2000A) on the left-hand-side through a conveyor input (247).Egg-depleted breeding material (246) is transferred onto the conveyor(245) of the egg transfer system (244) through a plurality of conveyorinputs (247A, 247B) so as to be configured to evenly distribute theenhanced feedstock on the conveyor (245). The wet enhanced feedstock(WEF) and the egg-depleted breeding material (246) are mixed together onthe surface of the conveyor (245) of the egg transfer system (244). Asthe conveyor motor (251) drives the conveyor (245) of the egg transfersystem (244).

Insects (225) within the insect feeding chamber (200) eat the wetenhanced feedstock (WEF) and lay eggs in the egg-depleted breedingmaterial (246) which are both present on the conveyor (245) of the eggtransfer system (244). The conveyor output (249) discharges a mixture ofwet enhanced feedstock (WEF) and egg-laden breeding material (250)towards an egg-laden breeding material conveyor (282B) for transfer to abreeding chamber (BC) within an insect breeding module (4000, 4000A,4000B, 4000C). A conveyor transfer bin (282A) is installed in betweenthe conveyor output (249) to funnel and direct the mixture of wetenhanced feedstock (WEF) and egg-laden breeding material (250) towardsthe egg-laden breeding material conveyor (282B).

An air supply fan (271) accepts an air supply (262) through an air vent(283) and passes it through an air heater (264) for delivery into theinterior (201) of the feeding chamber (200). A first access door (284)and a second access door (285) are installed on the fourth shippingcontainer side wall (CW-D). An insect evacuation output (205), that isconfigured to evacuate an insect and gas mixture (304) from the feedingchamber (200), is shown installed on the shipping container top wall(CW-T). The insect evacuation output (205) is connected to the feedingchamber exit conduit (302). The feeding chamber exit conduit (302) isconnected to the insect and gas mixture input (303) of the separator(300) within the insect evacuation module (3000). Each insect feedingmodule (2000, 2000A, 2000B, 2000C) may be equipped with a low voltagedisconnect switch (286) and a computer (COMP). The insect evacuationoutput (205) is equipped with a humidity sensor (208) and a firsttemperature sensor (210).

FIG. 28A:

FIG. 28A shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C).

FIG. 27B:

FIG. 27B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIGS. 27B and 28B show a front view and a side view of one non-limitingembodiment where a plurality of feeding chambers are provided in oneshipping container conforming to the International Organization forStandardization (ISO) specifications. In embodiments, the shippingcontainer of FIG. 27B and FIG. 28B are a 20 foot high. In embodiments,the shipping container of FIG. 27B and FIG. 28B are a 40 foot high.

FIG. 27B and FIG. 28B further elaborate upon FIG. 27A and FIG. 28Aexcept including a first feeding chamber (FC1, 200-1) and a secondfeeding chamber (FC2, 200-2) within the same shipping container. FIG.27B and FIG. 28B only show two feeding chambers (FC1, FC2) within oneshipping container, however it is to be noted that more than two mayalso be used as well.

The first feeding chamber (FC1) has a first insect evacuation output(205-1) and a feeding chamber first exit conduit (302-1) that areconfigured to discharge a first insect and gas mixture (304-1). Thesecond feeding chamber (FC2) has a second insect evacuation output(205-2) and a feeding chamber second exit conduit (302-2) that areconfigured to discharge a second insect and gas mixture (304-2). Thefirst feeding chamber (FC1) has a first side wall (202A), second sidewall (202B), third side wall (202C), and a fourth side wall (202D). Thesecond feeding chamber (FC2) has a first side wall (202AA), second sidewall (202BB), third side wall (202CC), and a fourth side wall (202DD).

As seen in FIG. 27B and FIG. 28B, the second side wall (202B) of thefirst feeding chamber (FC1) is the first side wall (202AA) of the secondfeeding chamber (FC2). The first feeding chamber (200-1) has a firstnetwork length (N-L1) and a first network width (N-W1). The secondfeeding chamber (200-2) has a second network length (N-L2) and a secondnetwork width (N-W2). The first feeding chamber (200-1) has a firstvibration unit connection (218A). The second feeding chamber (200-2) hasa second vibration unit connection (218B).

FIG. 27C:

FIG. 27C shows a top view of one embodiment of an insect feeding module(2000, 24000A, 2000B, 2000C) equipped with a humidity control unit(HCU).

FIG. 27C shows a non-limiting embodiment of a humidity control unit(HCU) positioned within the interior (201) of the feeding chamber (200).FIG. 27C also shows a humidity control unit (HCU) positioned within theinterior (201) of the feeding chamber (200, FC1, FC2, FC3) that iscontained within a shipping container.

In embodiments, the humidity control unit (HCU) includes a compressor(Q30), a condenser (Q32), a metering device (Q33), an evaporator (Q34),and a fan (Q35). The fan (Q35) may be equipped with a motor (Q36) and acontroller (Q37) that is configured to input or output a signal (Q38) toa computer (COMP).

In embodiments, the first growing assembly (100*) and/or the secondgrowing assembly (200*) are positioned within the interior (201) of thefeeding chamber (200). In embodiments, the first growing assembly (100*)having plants (107*) is positioned within the interior (201) of thefeeding chamber (200). In embodiments, the second growing assembly(200*) having plants (207*) is positioned within the interior (201) ofthe feeding chamber (200). In embodiments, the interior (ENC1) of theenclosure (ENC) of the Farming Superstructure System (FSS) (as disclosedin Volume II) is positioned within the interior (201) of the feedingchamber (201) of the Insect Production Superstructure System (IPSS) (asdisclosed on Volume I) to permit insects (225) to be co-located withinthe same interior (201, ENC1) the plants (107*, 207*).

The compressor (Q31) is connected to the condenser (Q32), the condenser(Q32) is connected to the metering device (Q33), the metering device(Q33) is connected to an evaporator (Q34), and the evaporator (Q34) isconnected to the compressor (Q31) to form a closed-loop refrigerationcircuit configured to contain a refrigerant (Q31). The metering device(Q33) includes one or more from the group consisting of a restriction,orifice, valve, tube, capillary, and capillary tube. The refrigerant(Q31) is conveyed from the compressor to the condenser, from thecondenser to the evaporator through the metering device, and from theevaporator to the compressor. The evaporator (Q34) is positioned toremove humidity from within the interior (201) of the feeding chamber(200, FC1, FC2, FC3) and is configured to evaporate refrigerant (Q31)within the evaporator (Q34) by removing heat from the interior (201) ofthe feeding chamber (200, FC1, FC2, FC3). In embodiments, a portion ofthe evaporator (Q34) is contained within the interior (201) of thefeeding chamber 200, FC1, FC2, FC3).

In embodiments, a portion of the evaporator (Q34) is contained withinthe interior (201) of an enclosure, such as a shipping container, thatthe feeding chamber (200, FC1, FC2, FC3) is positioned within. Inembodiments, the condenser (Q32) is not contained within the interior(201) of the feeding chamber (200, FC1, FC2, FC3). The fan (Q35) isconfigured to blow air from within the interior (201) of the feedingchamber (200, FC1, FC2, FC3) over at least a portion of the humiditycontrol unit (HCU).

The humidity control unit (HCU) is configured to selectively operate thesystem in a plurality of modes of operation, the modes of operationincluding at least:

(1) a first mode of operation in which compression of a refrigerant(Q31) takes place within the compressor (Q30), and the refrigerant (Q31)leaves the compressor (Q30) as a superheated vapor at a temperatureabove the condensing point of the refrigerant (Q31);

(2) a second mode of operation in which condensation of refrigerant(Q31) takes place within the condenser (Q32), heat is rejected and therefrigerant (Q31) condenses from a superheated vapor into a liquid, andthe liquid is cooled to a temperature below the boiling temperature ofthe refrigerant (Q31); and

(3) a third mode of operation in which evaporation of the refrigerant(Q31) takes place, and the liquid phase refrigerant (Q31) boils inevaporator (Q34) to form a vapor or a superheated vapor while absorbingheat from the interior (201) of the feeding chamber (200).

The evaporator (Q34) is configured to evaporate the refrigerant (Q31) toabsorb heat from the interior (201) of the feeding chamber (200). As aresult, the evaporator (Q34) may condense water from the interior (201)of the feeding chamber (200). In embodiments, the evaporator (Q34)condenses water vapor from the interior (201) of the feeding chamber(200) and forms condensate (Q39).

FIG. 27D:

FIG. 27DC shows one non-limiting embodiment where the compressor (Q30)within the humidity control unit (HCU) is that of a thermal compressor(Q30) that accepts a source of steam. The thermal compressor (Q30)accepts a tenth steam supply (LDS) that is provided from FIG. 14L. Alsoshown is in the thermal compressor (Q30) discharging a tenth condensate(LJC) to the condensate tank (LAP) shown on FIG. 14L.

FIG. 27E:

FIG. 27E shows one non-limiting embodiment where the compressor (Q30)within the humidity control unit (HCU) is that of a thermal compressor(Q30) that accepts a source of steam. The thermal compressor (Q30)accepts a tenth steam supply (LDS) that is provided from FIG. 14L. Alsoshown is in the thermal compressor (Q30) discharging a tenth condensate(LJC) to the condensate tank (LAP) shown on FIG. 14L.

In embodiments, the thermal compressor (Q30) (in both FIGS. 27E and 34B)includes a generator (Q50) and an absorber (Q60). The tenth steam supply(LDS), from FIG. 14L, is transferred from the steam distribution header(LCJ) and into the generator (Q50) of the thermal compressor (Q30). Inembodiments, a pump (Q45) connects the generator (Q50) to the absorber(Q60). Also, in embodiments, a metering device (Q55) connects theabsorber (Q60) to the generator (Q50). The metering device (Q55) mayinclude one or more from the group consisting of a restriction, orifice,valve, tube, capillary, and capillary tube.

Vapor-phase refrigerant is transferred from the evaporator (Q34) to theabsorber (Q60). The refrigerant transferred from the evaporator (Q34) tothe absorber (Q60) is then absorbed by an absorbent within the absorber(Q60). In embodiments, the refrigerant includes water or ammonia. Inembodiments, the absorbent includes lithium bromine or water.

A mixture of refrigerant and absorbent is transferred from the absorber(Q60) to the generator (Q50) via the pump (Q45). Heat in the form ofsteam (LDS) is transferred to the mixture of refrigerant and absorbentwithin the generator (Q50) to vaporize the refrigerant. The vapor-phase,or superheated vapor, refrigerant is transferred from the generator(Q50) to the condenser (Q32). The absorbent is transferred back to theabsorber (Q60) from the generator (Q50) through the metering device(Q55). In embodiments, the absorbent that is transferred through themetering device (Q55) takes a pressure drop. In embodiments, thegenerator (Q50) operates at a pressure that is greater than the pressurewithin the absorber (Q60).

In embodiments, the thermal compressor (Q30) may also be called anabsorption chiller. In embodiments, the thermal compressor may have onestage. In embodiments, the thermal compressor may have two stages. Inembodiments, electricity is required to power the pump (Q54). Inembodiments, the electricity that is required to power the pump (Q54)comes from the generator (LFH) shown in FIG. 14L.

FIG. 27F:

FIG. 27F elaborates upon FIG. 27E and shows one non-limiting embodimentwhere the compressor (Q30) within the humidity control unit (HCU) isthat of a thermal compressor (Q30) that accepts a source of heat, suchas flue gas (FG1). FIG. 27F (also applies to FIG. 34B) accepts a sourceof heat from the flue gas (FG1) transferred from FIG. 14L.

FIG. 28B:

FIG. 28B shows a top view of one embodiment of an insect feeding module(2000, 2000A, 2000B, 2000C) including a plurality of feeding chambersprovided in one shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

FIG. 29:

FIG. 29 shows a first side view of one embodiment of an insect feedingmodule (2000, 2000A, 2000B, 2000C).

FIG. 30:

FIG. 30 shows a front view of one embodiment of an insect evacuationmodule (3000). FIG. 30 shows a front view of one embodiment of an insectevacuation module (3000). Referring to FIGS. 30-32, the insectevacuation module (3000) is shown to be contained within a 40 feet highshipping container conforming to the International Organization forStandardization (ISO) specifications.

The insect evacuation module (3000) includes a plurality of separators(51, S2, S3) integrated with one common feeding chamber (FC1) as shownin FIGS. 27-29. FIGS. 30-32 shows the first separator (S1) as a firstinsect coarse separator (S1A), the second separator (S2) as a secondinsect fine separator (S2A), and the third separator (S3) as aparticulate separator (S3A). The first insect coarse separator (S1A) isconfigured to remove a portion of the insect portion (304A) separatedfrom the gas portion (304B) of an insect and gas mixture (304). Thesecond insect fine separator (S2A) is configured to remove insectssmaller than the insects separated in the first insect coarse separator(S1A). The particulate separator (S3A) is configured to removeparticulates such as remnants of enhanced feedstock, or fine polymerparticulate, for example, not only including pieces of portions ofinsect exoskeleton. The particulate separator (S3A) is in fluidcommunication with the polymer distribution module (1D) and isconfigured to transfer a portion of the separated particulate to thepolymer tank (1D2) as polymer (1D1).

First Separator (S1), First Insect Coarse Separator (S1A)

The first insect coarse separator (S1A) has a first insect coarseseparator input (S1A1) that is in fluid communication with the firstfeeding chamber insect evacuation output (205A) of the first feedingchamber (FC1) via a first feeding chamber exit conduit (302A). The firstinsect coarse separator (S1A) is configured to accept an insect and gasmixture (304) from the first feeding chamber (FC1), separate a portionof the insects from the gas and output a first insect-depleted gasstream (355) via a coarse separator gas and insect mixture output (356).

The first separator (S1) is equipped with a first dipleg (357), a firstseparator conveyor (358), and a first separator valve (361) interposedon the first dipleg (357). A first separated insect stream (360) isrouted down the first dipleg (357), through the first separator valve(361) and into the first separator conveyor (358). In embodiments, thefirst separator conveyor (358) is a compression screw (359) which servesto instantly kill insects by compressing them. The first separatedinsect stream (360) may in turn be transferred to an evacuated separatedinsect conveyor (378) via a first separator conveyor connection (379).

The evacuated separated insect conveyor (378) has a motor (378A) that isconfigured to transfer the first separated insect stream (360) to agrinder (1250) within an insect grinding module via a first separatedinsect stream input (371). In other embodiments, the first separatedinsect stream (360) may be sent to a pathogen removal unit (1550) withina pathogen removal module, or to a within a lipid extraction unit (1501)lipid extraction module.

Second Separator (S2), Second Insect Fine Separator (S2A)

The second insect fine separator (S2A) has a second insect fineseparator input (S2A1) that is in fluid communication with the coarseseparator gas and insect mixture output (356) of the first insect coarseseparator (S1A). The second insect fine separator (S2A) is configured toaccept a first insect-depleted gas stream (355) from the first insectcoarse separator (S1A), separate a portion of the insects from the gasand output a second insect-depleted gas stream (362) via a fineseparator gas and particulate mixture output (363).

The second separator (S2) is equipped with a second dipleg (364), asecond separator conveyor (365), and a second separator valve (368)interposed on the second dipleg (364). A second separated insect stream(360) is routed down the second dipleg (364), through the secondseparator valve (368) and into the second separator conveyor (365). Inembodiments, the second separator conveyor (365) is a compression screw(366) which serves to instantly kill insects by compressing them.

In embodiments, the second separator conveyor (365) is a not acompression screw (366) but instead routes the second separated insectstream (367) to the to a breeding chamber (BC) via a breeding chamberfine separated insect portion input (375). In embodiments, the secondseparator conveyor (365) is a not a compression screw (366) but insteadroutes the second separated insect stream (367) to a plurality of otherdestinations such as to the grinder (1250), pathogen removal unit(1550), or lipid extraction unit (1501). The second separated insectstream (367) may in turn be transferred to an evacuated separated insectconveyor (378) via a second separator conveyor connection (380) to forma combined first and second separator insect stream (381).

The combined first and second separator insect stream (381) is a mixtureof the first separated insect stream (360) and the second separatedinsect stream (367). The evacuated separated insect conveyor (378) has amotor (378A) that is configured to transfer the combined first andsecond separator insect stream (381) to a grinder (1250) within aninsect grinding module via a first separated insect stream input (371).In other embodiments, the first separated insect stream (360) may besent to a pathogen removal unit (1550) within a pathogen removal module,or to a within a lipid extraction unit (1501) lipid extraction module.

Third Separator (S3), Particulate Separator (S3A)

The particulate separator (S3A) has a particulate separator input (S3A1)that is in fluid communication with the fine separator gas andparticulate mixture output (363) of the second insect fine separator(S2A). The particulate separator (S3A) is configured to accept a secondinsect-depleted gas stream (362) from the second insect fine separator(S2A), separate a portion of the particulates from the gas and output aparticulate-depleted gas stream (369) to the insect evacuation fan(312).

The insect evacuation fan (312) is in fluid with the breeding chamber(BC) via a breeding chamber exhaust input (376) and is configured todischarge the exhaust (377) into the breeding chamber (BC). Inembodiments, the separated insect conveyor (328) of the third separator(S3) particulate separator (S3A) is in fluid communication with thepolymer distribution module (1D) and is configured to transfer a portionof the separated particulate stream (370) to the polymer tank (1D2) aspolymer (1D1).

In embodiments, the separated insect conveyor (328) of the thirdseparator (S3) particulate separator (S3A) is in fluid communicationwith the polymer distribution module (1D) and is configured to transfera portion of the separated particulate stream (370) to the polymer tank(1D2) as a polymer (1D1). The insect evacuation module (3000) isequipped with a first access door (386), second access door (387),computer (COMP), low voltage disconnect switch (388), and an air vent(389) that is configured to accept an air supply (390).

FIG. 31:

FIG. 31 shows a top view of one embodiment of an insect evacuationmodule (3000).

FIG. 32:

FIG. 32 shows a first side view of one embodiment of an insectevacuation module (3000).

FIG. 33:

FIG. 33 shows a front view of one embodiment of an insect breedingmodule (4000, 4000A, 4000B, 4000C). Referring to FIGS. 33-36, the insectbreeding module (4000, 4000A, 4000B, 4000C) is shown to be containedwithin a 40 feet high shipping container conforming to the InternationalOrganization for Standardization (ISO) specifications.

A feeding chamber 1 egg-laden breeding material transfer line (R1, 340)transfers egg-laden breeding material (250) via an egg-laden breedingmaterial conveyor (282B) into the insect breeding module (4000, 4000A)from the left-hand-side. Egg-laden breeding material (250), andoptionally a mixture of egg-laden breeding material (250) and a wetenhanced feedstock (WEF), are distributed onto a lower conveyor belt(415) of a first conveyor transfer unit (XY1A). The egg-laden breedingmaterial (250) being transferred to the interior (BCIN) of the breedingchamber 1 (BC1) where it is first elevated via a first conveyor transferunit (XY1A) to the first conveyor height (CH1A) of a first conveyor(CY1A) operating in a clockwise motion of operation.

In embodiments, the breeding chamber (BC) shown in FIGS. 33-36 representa typical breeding chamber 1 (BC1), breeding chamber 2 (BC2), breedingchamber 3 (BC3) as shown in FIG. 17. In embodiments, the first conveyortransfer unit (XY1A) takes the form of a vertical lift conveyor (409)including a lower conveyor unit (410) and an upper conveyor unit (411).The vertical lift conveyor (409) is equipped with a lift conveyor driveunit (419) that is configured to rotate the rollers within the lowerconveyor unit (410) and upper conveyor unit (411).

The lower conveyor unit (410) includes a first lower conveyor roller(412), second lower conveyor roller (413), third lower conveyor roller(414), and an endless lower conveyor belt (415) in communication witheach roller (412, 423, 414) and the lift conveyor drive unit (419). Theupper conveyor unit (411) includes a first upper conveyor belt roller(416), second upper conveyor roller (417), and an endless upper conveyorbelt (418) in communication with each roller (416, 417) and the liftconveyor drive unit (419).

Egg-laden breeding material (250), and optionally a mixture of egg-ladenbreeding material (250) and a wet enhanced feedstock (WEF) aredistributed onto the lower conveyor belt (415) of the lower conveyorunit (410). The breeding material and enhanced feedstock remnants aresandwiched in between the lower conveyor belt (415) of the lowerconveyor unit (410) and the upper conveyor belt (418) of the upperconveyor unit (411) and is elevated to the first conveyor height (CH1A)of a first conveyor (CY1A) operating in a clockwise motion of operation.

The first conveyor (CY1A) is positioned at a vertical height above atleast one other conveyor. FIGS. 33-36 shows five conveyors (CY1A, CY2A,CY3A, CY4A, CYSA) and the first conveyor (CY1A) is positioned at avertical height above each one of a second conveyor (CY2A), thirdconveyor (CY3A), fourth conveyor (CY4A), and fifth conveyor (CYSA). Thesecond conveyor (CY2A) is positioned at a vertical height above each oneof a third conveyor (CY3A), fourth conveyor (CY4A), and fifth conveyor(CYSA). The third conveyor (CY3A) is positioned at a vertical heightabove each one of a fourth conveyor (CY4A), and fifth conveyor (CYSA).The fourth conveyor (CY4A) is positioned at a vertical height above eachone of the fifth conveyor (CY5A).

The first conveyor (CY1A) is installed at a first conveyor height (CH1A)above the second conveyor (CY2A). The second conveyor (CY2A) isinstalled at a second conveyor height (CH2A) above the third conveyor(CY3A). The third conveyor (CY3A) is installed at a third conveyorheight (CH3A) above the fourth conveyor (CY4A). The fourth conveyor(CY4A) is installed at a fourth conveyor height (CH4A) above the fifthconveyor (CYSA).

FIG. 33-36 shows the first conveyor (CY1A), third conveyor (CY3A), fifthconveyor (CYSA) all configured to operate in a clockwise motion ofoperation. FIG. 33-36 shows the second conveyor (CY2A) and fourthconveyor (CY4A) configured to operate in a counter-clockwise motion ofoperation.

The first conveyor (CY1A) rotates in a clockwise motion about a firstconveyor first roller (P1) and a first conveyor second roller (P2). Thesecond conveyor (CY2A) rotates in a counter-clockwise motion about asecond conveyor first roller (P3) and a second conveyor second roller(P4). The third conveyor (CY3A) rotates in a clockwise motion about athird conveyor first roller (P5) and a third conveyor second roller(P6). The fourth conveyor (CY4A) rotates in a counter-clockwise motionabout a fourth conveyor first roller (P7) and a fourth conveyor secondroller (P8). The fifth conveyor (CYSA) rotates in a clockwise motionabout a fifth conveyor first roller (P9) and a fifth conveyor secondroller (P10).

A drive unit (404) is equipped with a motor (405) to drive a sprocket(406) and a roller (407). The drive unit (404) is operatively connectedto the first conveyor first roller (P1) of the first conveyor (CY1A),second conveyor second roller (P4) of the second conveyor (CY2A), thethird conveyor first roller (P5) of the third conveyor (CY3A), thefourth conveyor second roller (P8) of the fourth conveyor (CY4A), andthe fifth conveyor first roller (P9) of the fifth conveyor (CYSA).

Specifically, the sprocket (406) driven by the motor (405) of the driveunit (404) drives a roller chain (408) that is configured to operateeach conveyor (CY1A, CY2A, CY3A, CY4A, CYSA). The roller chain (408) isconfigured to interact with a roller chain support roller (P11) inbetween the first conveyor first roller (P1) and sprocket (406) of thedrive unit (404).

The circuit including the roller chain (408), sprocket (406), and driveunit (404) turns the fifth conveyor first roller (P9), third conveyorfirst roller (P5), and first conveyor first roller (P1) in the clockwisemotion. The circuit including the roller chain (408), sprocket (406),and drive unit (404) also turns the fourth conveyor second roller (P8)and second conveyor second roller (P4) in the counter-clockwise motion.

The first conveyor (CY1A) transfers a mixture of egg-laden breedingmaterial (250) and remnants of an enhanced feedstock to the secondconveyor (CY2A). The second conveyor (CY2A) transfers a mixture ofegg-laden breeding material (250) and remnants of an enhanced feedstock,and possibly hatched insects to the third conveyor (CY3A). The thirdconveyor (CY3A) transfers a mixture of egg-laden breeding material(250), remnants of an enhanced feedstock, and possibly hatched insectsto the fourth conveyor (CY4A). The fourth conveyor (CY4A) transfers amixture of egg-laden breeding material (250), remnants of an enhancedfeedstock, and possibly hatched insects to the fifth conveyor (CYSA).The fifth conveyor (CYSA) transfers a mixture of hatched insects,breeding material, and remnants of an enhanced feedstock to a hatchedinsect conveyor (402) and out of the insect breeding module (4000,4000A, 4000B, 4000C) via a feeding chamber 1 breeding chamber output(BC1B).

A conveyor transfer bin (401) is interposed in between the fifthconveyor (CY5A) and the hatched insect conveyor (402) to funnel anddirect a mixture of hatched insects, breeding material, and remnants ofan enhanced feedstock from the insect breeding module (4000, 4000A,4000B, 4000C) and into the hatched insect separation module (5000).

A conveyor side view (CSV) may be viewed in FIGS. 35-36 from the lengthalong the insect breeding module (4000) conveyor (CY1A, CY2A, CY3A,CY4A, CY5A). The insect breeding module (4000, 4000A, 4000B, 4000C) isequipped with a first access door (420), second access door (421), lowvoltage disconnect switch (422), temperature sensor (423), humiditysensor (425), and an air vent (427) configured to introduce an airsupply (428) to the interior (BCIN) of the breeding chamber (BC). Theinsect breeding module (4000, 4000A, 4000B, 4000C) may also be equippedwith a temperature control unit (429) to maintain a constant temperaturewith the interior (BCIN) of the breeding chamber (BC).

The first conveyor (CY1A) is equipped with a first hatched insectdetection sensor (OS1) to determine if insects have hatched and areactive on the surface of the first conveyor (CY1A). The second conveyor(CY2A) is equipped with a second hatched insect detection sensor (OS2)to determine if insects have hatched and are active on the surface ofthe second conveyor (CY2A). The third conveyor (CY3A) is equipped with athird hatched insect detection sensor (OS3) to determine if insects havehatched and are active on the surface of the third conveyor (CY3A). Thefourth conveyor (CY4A) is equipped with a fourth hatched insectdetection sensor (OS4) to determine if insects have hatched and areactive on the surface of the fourth conveyor (CY4A). The fifth conveyor(CY5A) is equipped with a fifth hatched insect detection sensor (OS5) todetermine if insects have hatched and are active on the surface of thefifth conveyor (CY5A). Either of the hatched insect detection sensors(OS1, 0S2, 0S3, 0S4, 0S5) may be an optical sensor, digital camera,motion sensor, active infrared (AIRs) sensor, passive infrared (PIRs)sensor, microwave motion sensor, continuous wave radar motion sensor(CW), vibration motion sensor, IR sensor, ultrasonic sensor, proximitysensor, and touch sensor, mass sensor, laser sensor, or the like.

FIG. 34:

FIG. 34 shows a top view of one embodiment of an insect breeding module(4000, 4000A, 4000B, 4000C). A side wall (403) may be positioned in theinsect breeding module (4000, 4000A, 4000B, 4000C) to permit access andmaintenance as shown in FIGS. 34-35. In embodiments, the side wall (403)is made up of a plastic, rubber, or an impermeable substance, such as atarp, curtain, cloth, or sheet and does not have openings in it. Inembodiments, the side wall (403) is made up of wire, screen, or meshthat is perforated with openings smaller than the average insect length(Ni-L) average insect width (Ni-W).

FIG. 34A:

FIG. 34A shows a top view of one embodiment of an insect breeding module(4000, 4000A, 4000B, 4000C) equipped with a humidity control unit (HCU).

FIG. 34A shows a non-limiting embodiment of a humidity control unit(HCU) positioned within the interior (BCIN) of the breeding chamber(BC). FIG. 36A also shows a humidity control unit (HCU) positionedwithin the interior (BCIN) of the breeding chamber (BC) that iscontained within a shipping container.

In embodiments, the humidity control unit (HCU) includes a compressor(QQ30), a condenser (QQ32), a metering device (QQ33), an evaporator(Q34), and a fan (Q35). The fan (Q35) may be equipped with a motor(QQ36) and a controller (QQ37) that is configured to input or output asignal (QQ38) to a computer (COMP).

The compressor (QQ31) is connected to the condenser (QQ32), thecondenser (QQ32) is connected to the metering device (QQ33), themetering device (QQ33) is connected to an evaporator (QQ34), and theevaporator (QQ34) is connected to the compressor (QQ31) to form aclosed-loop refrigeration circuit configured to contain a refrigerant(QQ31). The metering device (QQ33) includes one or more from the groupconsisting of a restriction, orifice, valve, tube, capillary, andcapillary tube. The refrigerant (QQ31) is conveyed from the compressorto the condenser, from the condenser to the evaporator through themetering device, and from the evaporator to the compressor. Theevaporator (QQ34) is positioned to remove humidity from within theinterior (BCIN) of the breeding chamber (BC) and is configured toevaporate refrigerant (QQ31) within the evaporator (QQ34) by removingheat from the interior (BCIN) of the breeding chamber (BC). Inembodiments, a portion of the evaporator (QQ34) is contained within theinterior (BCIN) of the breeding chamber (BC).

In embodiments, a portion of the evaporator (QQ34) is contained withinthe interior (BCIN) of an enclosure, such as a shipping container, thatthe breeding chamber (BC) is positioned within. In embodiments, thecondenser (QQ32) is not contained within the interior (BCIN) of thebreeding chamber (BC). The fan (QQ35) is configured to blow air fromwithin the interior (BCIN) of the breeding chamber (BC) over at least aportion of the humidity control unit (HCU).

The humidity control unit (HCU) is configured to selectively operate thesystem in a plurality of modes of operation, the modes of operationincluding at least:

(1) a first mode of operation in which compression of a refrigerant(QQ31) takes place within the compressor (QQ30), and the refrigerant(QQ31) leaves the compressor (QQ30) as a superheated vapor at atemperature above the condensing point of the refrigerant (QQ31);

(2) a second mode of operation in which condensation of refrigerant(QQ31) takes place within the condenser (QQ32), heat is rejected and therefrigerant (QQ31) condenses from a superheated vapor into a liquid, andthe liquid is cooled to a temperature below the boiling temperature ofthe refrigerant (QQ31); and

(3) a third mode of operation in which evaporation of the refrigerant(QQ31) takes place, and the liquid phase refrigerant (QQ31) boils inevaporator (QQ34) to form a vapor or a superheated vapor while absorbingheat from the interior (BCIN) of the breeding chamber (BC).

The evaporator (QQ34) is configured to evaporate the refrigerant (QQ31)to absorb heat from the interior (BCIN) of the breeding chamber (BC). Asa result, the evaporator (QQ34) may condense water from the interior(BCIN) of the breeding chamber (BC). In embodiments, the evaporator(QQ34) condenses water vapor from the interior (BCIN) of the breedingchamber (BC) and forms condensate (QQ39).

FIG. 34B:

FIG. 34B shows one non-limiting embodiment where the compressor (QQ30)within the humidity control unit (HCU) is that of a thermal compressor(QQ30) that accepts a source of steam. The thermal compressor (QQ30)accepts an eleventh steam supply (LDV) that is provided from FIG. 14L.Also shown is the thermal compressor (QQ30) discharging an eleventhcondensate (LJD) to the condensate tank (LAP) shown on FIG. 14L.

FIG. 35:

FIG. 35 shows a first side view of one embodiment of an insect breedingmodule (4000, 4000A) at a cutaway section of the conveyor side view(CSV). In embodiments, the breeding chamber (BC) includes a plurality ofconveyors including a first conveyor (CY1A), second conveyor (CY2A),third conveyor (CY3A), fourth conveyor (CY4A), and fifth conveyor (CY5A)that are operatively rotated by a plurality of rollers including a firstconveyor first roller (P1), second conveyor second roller (P4), thirdconveyor first roller (P5), fourth conveyor second roller (P8), andfifth conveyor first roller (P9).

FIG. 36:

FIG. 36 shows an embodiment of the insect breeding module (4000, 4000A,4000B, 4000C) from the conveyor side view (CSV). A side wall (403) maybe positioned within the insect breeding module (4000, 4000A, 4000B,4000C) to permit a plurality of breeding trains within one sinceshipping container to be separated apart from the temperature controlunit (429). Three separate breeding chamber conveyor trains areillustrated with a side wall (403) positioned to space-apart thebreeding chamber conveyor trains (BCT1, BCT2, BCT3) from the temperaturecontrol unit (429).

A first breeding chamber conveyor train (BCT1) includes a plurality ofconveyors driven by a plurality of rollers including a first conveyorfirst roller (P1), second conveyor second roller (P4), third conveyorfirst roller (P5), fourth conveyor second roller (P8), and fifthconveyor first roller (P9). A second breeding chamber conveyor train(BCT2) includes a plurality of conveyors driven by a plurality ofrollers including a first conveyor first roller (P1B), second conveyorsecond roller (P4B), third conveyor first roller (P5B), fourth conveyorsecond roller (P8B), and a fifth conveyor first roller (P9B). A thirdbreeding chamber conveyor train (BCT3) includes a plurality of conveyorsdriven by a plurality of rollers including a first conveyor first roller(P1C), second conveyor second roller (P4C), third conveyor first roller(P5C), fourth conveyor second roller (P8C), and fifth conveyor firstroller (P9C).

FIG. 37:

FIG. 37 shows a front view of one embodiment of a hatched insectseparation module (5000, 5000A, 5000B, 5000C). Referring to FIGS. 37-39,the hatched insect separation module (5000, 5000A, 5000B, 5000C) isshown to be contained within a 40 feet high shipping containerconforming to the International Organization for Standardization (ISO)specifications.

FIGS. 37-39 shows the hatched insect separation module (5000) equippedwith a breeding material and insect separator (SEPIA) and a breedingmaterial tank (500). A hatched insect conveyor (402) transfers a mixtureof hatched insects, breeding material, and remnants of an enhancedfeedstock into a breeding material and insect separator (SEPIA) via ahatched insect and breeding material input (515).

The breeding material and insect separator (SEPIA) includes an interior(SIN1), a separator input (1SEPA), a separator material output (1SEPB),and a separator insect output (1SEPC). The breeding material and insectseparator (SEPIA) is connected to breeding chamber 1 (BC1) via abreeding chamber 1 hatched egg and breeding material transfer line (U1).The breeding chamber 1 hatched egg and breeding material transfer line(U1) is connected at one end to the breeding chamber 1 (BC1) via afeeding chamber 1 breeding chamber output (BC1B) and connected atanother end to the breeding material and insect separator (SEPIA) via aseparator input (1SEPA).

The breeding material and insect separator (SEPIA) is equipped with adipleg (517) to transfer an egg-depleted material (518) to anegg-depleted material transfer conveyor (519). The egg-depleted materialtransfer conveyor (519) is equipped with a motor (520) and is configuredto transfer separated breeding material (523) to the interior (501) ofthe breeding material tank (500) via a material transfer line (522). Thematerial transfer line (522) is connected at one end to the egg-depletedmaterial transfer conveyor (519) and at another rend to the breedingmaterial input (502) of the breeding material tank (500).

The separator input (1SEPA) is configured to accept hatched insects andbreeding material from the fifth conveyor (CYSA) of breeding chamber 1(BC1), and separate hatched insects (400) from the breeding material(523). The separator insect output (1SEPC) is configured to dischargehatched insects (400) from the interior (SIN1) of the breeding materialand insect separator (SEPIA) and route the hatched insects (400) toeither one of a plurality of feeding chambers (FC1, FC2, FC3) via aseparator hatched insect transfer line (01). Specifically, separatorinsect output (1SEPC) is configured to discharge hatched insects (400)first feeding chamber (FC1), or to the second feeding chamber (FC2), orto the third feeding chamber (FC3). Hatched insects (400) transferredfrom the hatched insect separation module (5000) to the insect feedingmodule (2000) are made available to the first feeding chamber (FC1) viaa first hatched insect output (DFC).

The breeding material tank (500) has an interior (501), a breedingmaterial input (502), and a breeding material output (510). Breedingmaterial, and remnants of an enhanced feedstock may be transferred fromthe breeding material and insect separator (SEPIA) interior (501) of thebreeding material tank (500) through a breeding material input (502).Breeding material, and remnants of an enhanced feedstock may besubstantially evenly distributed to the interior (501) of the breedingmaterial tank (500) via a breeding material input distributor (502A).

The breeding material tank (500) also has a top section (503), a bottomsection (506), and an interior (501) defined by at least one side wall(507). A breeding material screw conveyor (508) is located at the bottomsection (506) and configured to transfer breeding material to either oneof a plurality of feeding chambers (FC1, FC2, FC3) via a breedingmaterial transfer line (511). The breeding material transfer line (511)is connected at one end to any one of a plurality of feeding chambers(FC1, FC2, FC3) and connected at another end to the breeding materialscrew conveyor (508) via a breeding material output (510). The breedingmaterial screw conveyor (508) is equipped with a breeding material screwconveyor motor (512). The hatched insect separation module (5000) isequipped with a first access door (528), second access door (529), lowvoltage disconnect switch (530), and a computer (COMP). In embodiments,the breeding material is heated prior to being introduced to the insectfeeding chamber. In embodiments, the breeding material is sterilized byheat prior to being introduced to the insect feeding chamber.

FIG. 38:

FIG. 38 shows a top view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 39:

FIG. 39 shows a first side view of one embodiment of a hatched insectseparation module (5000, 5000A).

FIG. 40A:

FIG. 40 shows Table 1 with upper and lower ranges of feedstock mineralenhancers, feedstock vitamin enhancers, feedstock polymer enhancers, andother ‘energy-Insect®’ enhancers.

FIG. 40B:

FIG. 40B shows one non-limiting example of process conditions within anInsect Production Superstructure System (IPSS). Table 2 of FIG. 40Blists process conditions including the following: Feeding ChamberTemperature ranges from between about 60 degrees Fahrenheit to about 94degrees Fahrenheit; Breeding Chamber Temperature ranges from betweenabout 64 degrees Fahrenheit to about 90 degrees Fahrenheit; BreedingChamber Residence Time ranges from between about 1 week to about 5weeks; Feeding Chamber Humidity ranges from between about 25 percenthumidity to about 100 percent humidity; Breeding Chamber Humidity rangesfrom between about 50 percent humidity to about 100 percent humidity;average insect mass ranges from between about 0.2 grams to about 0.907grams; quantity of insects per pound ranges from between about 2268insects to about 500 insects; tons of insects per cycle ranges frombetween about 0.5 ton to about 1 ton; quantity of insects per cycleranges from between about 2,267,950 to about 1,000,000; and, durationper cycle ranges from between about 1 week to about 5 weeks. Inembodiments, a cycle may be defined as the duration of time when insectsare grown within the feeding chamber or plurality of feeding chambers.

In embodiments, the average insect mass ranges from between 0.10 gramsto 0.15 grams, 0.15 grams to 0.20 grams, 0.20 grams to 0.25 grams, 0.25grams to 0.30 grams, 0.30 grams to 0.35 grams, 0.35 grams to 0.40 grams,0.40 grams to 0.45 grams, 0.45 grams to 0.50 grams, 0.50 grams to 0.55grams, 0.55 grams to 0.60 grams, 0.60 grams to 0.65 grams, 0.65 grams to0.70 grams, 0.70 grams to 0.75 grams, 0.75 grams to 0.80 grams, 0.80grams to 0.85 grams, 0.85 grams to 0.90 grams, 0.90 grams to 0.95 grams,0.95 grams to 1.00 grams, 1.00 grams to 1.50 grams, 1.50 grams to 2.00grams, 2.00 grams to 2.50 grams, 2.50 grams to 3.00 grams, 3.00 grams to3.50 grams, 3.50 grams to 4.00 grams, 4.00 grams to 4.50 grams, 4.50grams to 5.00 grams, 5.00 grams to 6.00 grams, 6.00 grams to 7.00 grams,7.00 grams to 8.00 grams, 8.00 grams to 9.00 grams, or 9.00 grams to10.00 grams.

In embodiments, the average insect mass ranges from between 0.001 gramsto 0.002 grams, 0.002 grams to 0.003 grams, 0.003 grams to 0.004 grams,0.004 grams to 0.005 grams, 0.005 grams to 0.006 grams, 0.006 grams to0.007 grams, 0.007 grams to 0.008 grams, 0.008 grams to 0.009 grams,0.009 grams to 0.010 grams, 0.010 grams to 0.015 grams, 0.015 grams to0.020 grams, 0.020 grams to 0.025 grams, 0.025 grams to 0.030 grams,0.030 grams to 0.035 grams, 0.035 grams to 0.040 grams, 0.040 grams to0.045 grams, 0.045 grams to 0.050 grams, 0.050 grams to 0.055 grams,0.055 grams to 0.060 grams, 0.060 grams to 0.065 grams, 0.065 grams to0.070 grams, 0.070 grams to 0.075 grams, 0.075 grams to 0.080 grams,0.080 grams to 0.085 grams, 0.085 grams to 0.090 grams, 0.090 grams to0.095 grams, or 0.095 grams to 0.100 grams.

In embodiments, the quantity of insects per pound ranges from between 45to 55, 55 to 65, 65 to 75, 75 to 85, 85 to 95, 95 to 105, 105 to 115,115 to 125, 125 to 150, 150 to 200, 200 to 300, 300 to 400, 400 to 500,500 to 600, 600 to 700, 700 to 800, 800 to 900, 900 to 1000, 1000 to1250, 1250 to 1500, 1500 to 1750, 1750 to 2000, 2000 to 2250, 2250 to2500, 2500 to 3000, 3000 to 3500, 3500 to 4000, 4000 to 4500, 4500 to5000, 5000 to 6000, 6000 to 7000, 7000 to 8000, 8000 to 9000, 9000 to10000, 10000 to 20000, 20000 to 30000, 30000 to 40000, 40000 to 50000,50000 to 100000, 100000 to 150000, 150000 to 200000, 200000 to 250000,250000 to 300000, 300000 to 350000, 350000 to 400000, 400000 to 450000,450000 to 500000, 500000 to 600000, 600000 to 700000, 700000 to 800000,800000 to 900000, or 900000 to 1000000.

FIG. 40C:

FIG. 40C shows nutritional requirements of insects produced in an InsectProduction Superstructure System (IPSS) that are fed an enhancedfeedstock. Table 3 of FIG. 40C lists nutritional information for insectsfed an enhanced feedstock within an Insect Production SuperstructureSystem (IPSS) including the following: energy content ranges frombetween about 4.5 British Thermal Units (BTU) per pound to about 10.5BTU per pound; protein content ranges from between about 45 weightpercent to about 85 weight percent; carbon content ranges from betweenabout 15 weight percent to about 55 weight percent; oxygen contentranges from between about 15 weight percent to about 55 weight percent;hydrogen content ranges from between about 2.5 weight percent to about20 weight percent; carbohydrate content ranges from between about 3.5weight percent to about 13 weight percent; ash content ranges frombetween about 2.5 weight percent to about 7.5 weight percent; watercontent ranges from between about 2 weight percent to about 10 weightpercent; total fat content ranges from between about 5 weight percent toabout 60 weight percent; palmitic acid content ranges from between about5 weight percent to about 60 weight percent; linoleic acid contentranges from between about 5 weight percent to about 60 weight percent;alpha-linoleic acid content ranges from between about 5 weight percentto about 60 weight percent; oleic acid content ranges from between about5 weight percent to about 60 weight percent; gamma-linoleic acid contentranges from between about 5 weight percent to about 60 weight percent;stearic acid content ranges from between about 5 weight percent to about60 weight percent; potassium content ranges from between about 25 ppm toabout 1 weight percent; chloride content ranges from between about 50ppm to about 1 weight percent; calcium content ranges from between about50 ppm to about 1 weight percent; phosphorous content ranges frombetween about 50 ppm to about 1 weight percent; magnesium content rangesfrom between about 50 ppm to about 1 weight percent; zinc content rangesfrom between about 50 ppm to about 1 weight percent; iron content rangesfrom between about 25 ppm to about 1500 ppm; sodium content ranges frombetween about 1500 ppm to about 5500 ppm; manganese content ranges frombetween about 50 ppm to about 1 weight percent; copper content rangesfrom between about 50 ppm to about 1 weight percent; iodine contentranges from between about 50 ppm to about 1 weight percent; seleniumcontent ranges from between about 50 ppm to about 1 weight percent;molybdenum content ranges from between about 50 ppm to about 1 weightpercent; Vitamin B1 content ranges from between about 15 ppm to about 15weight percent; Vitamin B2 content ranges from between about 15 ppm toabout 15 weight percent; Vitamin B12 content ranges from between about15 ppm to about 15 weight percent; Vitamin E content ranges from betweenabout 15 ppm to about 15 weight percent; Vitamin A content ranges frombetween about 15 ppm to about 15 weight percent; niacin content rangesfrom between about 50 ppm to about 5 weight percent; taurine contentranges from between about 50 ppm to about 5 weight percent; glucuronicacid content ranges from between about 50 ppm to about 5 weight percent;malic acid content ranges from between about 50 ppm to about 5 weightpercent; N-acetyl L tyrosine content ranges from between about 50 ppm toabout 5 weight percent; L-phenylalanine content ranges from betweenabout 50 ppm to about 5 weight percent; caffeine content ranges frombetween about 50 ppm to about 5 weight percent; citicoline contentranges from between about 50 ppm to about 5 weight percent; insect bulkdensity ranges from between about 3.5 pounds per cubic foot to about14.999 pounds per cubic foot; ground insect bulk density ranges frombetween about 15 pounds per cubic foot to about 50 pounds per cubicfoot.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also include: a bacteria content rangingfrom between: 0.05 colony-forming units per gram (CFU/g) to 0.100 CFU/g,0.1 CFU/g to 0.2 CFU/g, 0.2 CFU/g to 0.4 CFU/g, 0.4 CFU/g to 0.8 CFU/g,0.8 CFU/g to 1.6 CFU/g, 1.6 CFU/g to 3.2 CFU/g, 3.2 CFU/g to 6.4 CFU/g,6.4 CFU/g to 12.8 CFU/g, 12.8 CFU/g to 25 CFU/g, 25 CFU/g to 50 CFU/g,50 CFU/g to 100 CFU/g, 100 CFU/g to 200 CFU/g, 200 CFU/g to 400 CFU/g,400 CFU/g to 800 CFU/g, 800 CFU/g to 1,600 CFU/g, 1,600 CFU/g to 3,200CFU/g, 3,200 CFU/g to 6,400 CFU/g, 32,000 CFU/g to 320,000 CFU/g,320,000 CFU/g to 3,200,000 CFU/g, 3,200,000 CFU/g to 32,000,000 CFU/g.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also include: a fungus content ranging frombetween: 0.05 colony-forming units per gram (CFU/g) to 0.100 CFU/g, 0.1CFU/g to 0.2 CFU/g, 0.2 CFU/g to 0.4 CFU/g, 0.4 CFU/g to 0.8 CFU/g, 0.8CFU/g to 1.6 CFU/g, 1.6 CFU/g to 3.2 CFU/g, 3.2 CFU/g to 6.4 CFU/g, 6.4CFU/g to 12.8 CFU/g, 12.8 CFU/g to 25 CFU/g, 25 CFU/g to 50 CFU/g, 50CFU/g to 100 CFU/g, 100 CFU/g to 200 CFU/g, 200 CFU/g to 400 CFU/g, 400CFU/g to 800 CFU/g, 800 CFU/g to 1,600 CFU/g, 1,600 CFU/g to 3,200CFU/g, 3,200 CFU/g to 6,400 CFU/g, 32,000 CFU/g to 320,000 CFU/g,320,000 CFU/g to 3,200,000 CFU/g, 3,200,000 CFU/g to 32,000,000 CFU/g.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: an alanine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: an arginine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: an aspartic acid contentranging from between: 500 parts per million to 1000 parts per million,1000 parts per million to 5000 parts per million, 5000 parts per millionto 7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a glutamic acid contentranging from between: 500 parts per million to 1000 parts per million,1000 parts per million to 5000 parts per million, 5000 parts per millionto 7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a glycine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a histidine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: an isoleucine contentranging from between: 500 parts per million to 1000 parts per million,1000 parts per million to 5000 parts per million, 5000 parts per millionto 7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a leucine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a lysine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a proline content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a serine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a threonine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a tyrosine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a valine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also include: a pH ranging from between:6.00 to 6.05, 6.05 to 6.10, 6.10 to 6.15, 6.15 to 6.20, 6.20 to 6.25,6.25 to 6.30, 6.30 to 6.35, 6.35 to 6.40, 6.40 to 6.45, 6.45 to 6.50,6.50 to 6.55, 6.55 to 6.60, 6.60 to 6.65, 6.65 to 6.70, 6.70 to 6.75,6.75 to 6.80, 6.80 to 6.85, 6.85 to 6.90, 6.90 to 6.95, 6.95 to 7.00,7.00 to 7.05, 7.05 to 7.10, 7.10 to 7.15, 7.15 to 7.20, 7.20 to 7.25,7.25 to 7.30, 7.30 to 7.35, 7.35 to 7.40, 7.40 to 7.45, 7.45 to 7.50,7.50 to 7.55, 7.55 to 7.60, 7.60 to 7.65, 7.65 to 7.70, 7.70 to 7.75,7.75 to 7.80, 7.80 to 7.85, 7.85 to 7.90, 7.90 to 7.95, 7.95 to 8.00,8.00 to 8.05, 8.05 to 8.10, 8.10 to 8.15, 8.15 to 8.20, 8.20 to 8.25,8.25 to 8.30, 8.30 to 8.35, 8.35 to 8.40, 8.40 to 8.45, or 8.45 to 8.50.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also includes: a water activity (Aw)ranging from between: 0.05 to 0.1, 0.1 to 0.15, 0.15 to 0.2, 0.2 to0.25, 0.25 to 0.3, 0.3 to 0.35, 0.35 to 0.4, 0.4 to 0.45, 0.45 to 0.5,0.5 to 0.55, or 0.55 to 0.6.

In embodiments, the insects produced in an Insect ProductionSuperstructure System (IPSS) also include: a carotenoid contentincluding one or more ranges selected from the group consisting of: 5.0μg/g to 7.5 μg/g, 7.5 μg/g to 10.0 μg/g, 10.0 μg/g to 12.5 μg/g, 12.5μg/g to 15.0 μg/g, 15.0 μg/g to 17.5 μg/g, 17.5 μg/g to 20.0 μg/g, 20.0μg/g to 22.5 μg/g, 22.5 μg/g to 25.0 μg/g, 25.0 μg/g to 27.5 μg/g, 27.5μg/g to 30.0 μg/g, 30.0 μg/g to 32.5 μg/g, 32.5 μg/g to 35.0 μg/g, 35.0μg/g to 37.5 μg/g, 37.5 μg/g to 40.0 μg/g, 40.0 μg/g to 42.5 μg/g, 42.5μg/g to 45.0 μg/g, 45.0 μg/g to 47.5 μg/g, 47.5 μg/g to 50.0 μg/g, 50.0μg/g to 52.5 μg/g, 52.5 μg/g to 55.0 μg/g, 55.0 μg/g to 57.5 μg/g, 57.5μg/g to 60.0 μg/g, 60.0 μg/g to 62.5 μg/g, 62.5 μg/g to 65.0 μg/g, 65.0μg/g to 67.5 μg/g, 67.5 μg/g to 70.0 μg/g, 70.0 μg/g to 72.5 μg/g, 72.5μg/g to 75.0 μg/g, 75.0 μg/g to 77.5 μg/g, 77.5 μg/g to 80.0 μg/g, 80.0μg/g to 82.5 μg/g, 82.5 μg/g to 85.0 μg/g, 85.0 μg/g to 87.5 μg/g, 87.5μg/g to 90.0 μg/g, 90.0 μg/g to 92.5 μg/g, 92.5 μg/g to 95.0 μg/g, 95.0μg/g to 97.5 μg/g, and 97.5 μg/g to 100.0 μg/g;

wherein:

the carotenoid includes one or more carotenoids selected from the groupconsisting of: antheraxanthin, astaxanthin, auroxanthin, bixin,canthaxanthin, capsanthin, capsorubin, α-carotene, β-carotene,β-carotene-5,6-epoxide, β-carotene-5,8-epoxide (mutatochrome),β-carotene-5,6,5′,6′-diepoxide, δ-carotene, γ-carotene, ζ-carotene,crocetin, α-cryptoxanthin, β-cryptoxanthin, echinenone, lutein,lutein-5,6-epoxide (taraxanthin), lycopene, neoxanthin, neurosporene,phytoene, phytofluene, rubixanthin, violaxanthin, α-zeacarotene,β-zeacarotene, zeaxanthin, and zeinoxanthin.

FIG. 41A:

FIG. 41A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing an insect feeding chamber having egg-laying insectspresent therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) introducing said enhanced feedstock into said insect feeding chamberto feed the egg-laying insects present therein;

(d) removing a portion of said egg-laying insects from said insectfeeding chamber by applying a vacuum with a velocity pressure range fromabout 0.001 inches of water to about 400 inches of water and at velocityfrom about 0.05 feet per second to about 1500 feet per second. Inembodiments, the insect feeding chamber may operate at an enhancedfeedstock to insect ratio ranging from between about 1 ton of enhancedfeedstock per ton of insects produced to about 5 tons of enhancedfeedstock per ton of insects produced. In embodiments, the feedingchamber operates at a temperature ranging from between 50 degreesFahrenheit to about 120 degrees Fahrenheit. In embodiments, the feedingchamber operates at a pressure ranging from between 12 psia to about 16psia.

FIG. 41B:

FIG. 41B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing an insect feeding chamber having egg-laying insectspresent therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) introducing said enhanced feedstock into said insect feeding chamberto feed the egg-laying insects present therein;

(d) removing a portion of said egg-laying insects from said insectfeeding chamber by vibrating at least a portion of said insect feedingchamber. In embodiments, the insect feeding chamber may operate at anenhanced feedstock to insect ratio ranging from between about 1 ton ofenhanced feedstock per ton of insects produced to about 5 tons ofenhanced feedstock per ton of insects produced. In embodiments, thefeeding chamber operates at a temperature ranging from between 50degrees Fahrenheit to about 120 degrees Fahrenheit. In embodiments, thefeeding chamber operates at a pressure ranging from between 12 psia toabout 16 psia.

FIG. 42A:

FIG. 42A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing an insect feeding chamber having egg-laying insectspresent therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) introducing said enhanced feedstock into said insect feeding chamberto feed the egg-laying insects present therein;

(d) removing at least a portion of eggs laid by the egg-laying insects;

(e) incubating at least a portion of the removed eggs;

(f) hatching at least a portion of incubated eggs;

(g) introducing a portion of hatched insects into said insect feedingchamber;

(h) removing a portion of said egg-laying insects said insect feedingchamber by applying a vacuum with a velocity pressure range from about0.001 inches of water to about 400 inches of water and at velocity fromabout 0.05 feet per second to about 1500 feet per second.

FIG. 42B:

FIG. 42B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing an insect feeding chamber having egg-laying insectspresent therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) introducing said enhanced feedstock into said insect feeding chamberto feed the egg-laying insects present therein;

(d) removing at least a portion of eggs laid by the egg-laying insects;

(e) incubating at least a portion of the removed eggs;

(f) hatching at least a portion of incubated eggs;

(g) introducing a portion of hatched insects into said insect feedingchamber;

(h) removing a portion of said egg-laying insects from said insectfeeding chamber by vibrating at least a portion of said insect feedingchamber.

FIG. 43A:

FIG. 43A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams; (d) introducing said plurality of enhanced feedstockstreams into said plurality of insect feeding chambers to feed theegg-laying insects present therein;

(e) removing at least a portion of eggs laid by the egg-laying insects;

(f) incubating at least a portion of the removed eggs;

(g) hatching at least a portion of incubated eggs;

(h) introducing a portion of hatched insects into at least one of theplurality of insect feeding chambers;

(i) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers by applying a vacuum with a velocity pressurerange from about 0.001 inches of water to about 400 inches of water andat velocity from about 0.05 feet per second to about 1500 feet persecond.

FIG. 43B:

FIG. 43B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams;

(d) introducing said plurality of enhanced feedstock streams into saidplurality of insect feeding chambers to feed the egg-laying insectspresent therein;

(e) removing at least a portion of eggs laid by the egg-laying insects;

(f) incubating at least a portion of the removed eggs;

(g) hatching at least a portion of incubated eggs;

(h) introducing a portion of hatched insects into at least one of theplurality of insect feeding chambers;

(i) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers by vibrating at least a portion of saidplurality of insect feeding chambers.

FIG. 44A:

FIG. 44A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects of said order present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams;

(d) introducing said plurality of enhanced feedstock streams into saidplurality of insect feeding chambers to feed the egg-laying insectspresent therein; and,

(e) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers by applying a vacuum with a velocity pressurerange from about 0.001 inches of water to about 400 inches of water andat velocity from about 0.05 feet per second to about 1500 feet persecond. In embodiments, the insect feeding chamber may operate at anenhanced feedstock to insect ratio ranging from between about 1 ton ofenhanced feedstock per ton of insects produced to about 5 tons ofenhanced feedstock per ton of insects produced. In embodiments, thefeeding chamber operates at a temperature ranging from between 50degrees Fahrenheit to about 120 degrees Fahrenheit. In embodiments, thefeeding chamber operates at a pressure ranging from between 12 psia toabout 16 psia.

FIG. 44B:

FIG. 44B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects. In embodiments, the present disclosuredescribes a method for raising Orthoptera order of insects, the methodcomprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects of said order present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams;

(d) introducing said plurality of enhanced feedstock streams into saidplurality of insect feeding chambers to feed the egg-laying insectspresent therein; and,

(e) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers by vibrating at least a portion of saidplurality of insect feeding chambers.

In embodiments, the insect feeding chamber may operate at an enhancedfeedstock to insect ratio ranging from between about 1 ton of enhancedfeedstock per ton of insects produced to about 5 tons of enhancedfeedstock per ton of insects produced. In embodiments, the feedingchamber operates at a temperature ranging from between 50 degreesFahrenheit to about 120 degrees Fahrenheit. In embodiments, the feedingchamber operates at a pressure ranging from between 12 psia to about 16psia.

FIG. 45A:

FIG. 45A shows one non-limiting embodiment of a method for raisingOrthoptera order of insects to generate a multifunctional composition.In embodiments, the present disclosure describes a method for raisingOrthoptera order of insects to generate a multifunctional composition,the method comprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams;

(d) introducing said plurality of enhanced feedstock streams into saidplurality of insect feeding chambers to feed the egg-laying insectspresent therein;

(e) removing at least a portion of eggs laid by the egg-laying insects;

(f) incubating at least a portion of the removed eggs;

(g) hatching at least a portion of incubated eggs;

(h) introducing a portion of hatched insects into at least one of theplurality of insect feeding chambers;

(i) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers;

(j) grinding a portion of the removed insects to form a stream of groundinsects;

(k) creation of a multifunctional composition by mixing ground insectsof step (j) with one or more ingredients from the group consisting offiber-starch materials, binding agents, density improving texturalsupplements, moisture improving textural supplements, and cannabisenhancers.

FIG. 45B:

FIG. 45B shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional composition.In embodiments, the present disclosure describes a method for raisingOrthoptera order of insects to generate a multifunctional composition,the method comprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams; introducing said plurality of enhanced feedstockstreams into said plurality of insect feeding chambers to feed theegg-laying insects present therein;

(d) removing at least a portion of eggs laid by the egg-laying insects;

(e) incubating at least a portion of the removed eggs;

(f) hatching at least a portion of incubated eggs;

(g) introducing a portion of hatched insects into at least one of theplurality of insect feeding chambers;

(h) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers;

(i) removing pathogens from a portion of the removed insects to form astream of pathogen-depleted insects;

(j) creation of a multifunctional composition by mixing a portion of thestream of pathogen-depleted insects of step (i) with one or moreingredients from the group consisting of fiber-starch materials, bindingagents, density improving textural supplements, moisture improvingtextural supplements, and cannabis enhancers.

FIG. 46:

FIG. 46 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects to generate a multifunctional composition.In embodiments, the present disclosure describes a method for raisingOrthoptera order of insects to generate a multifunctional composition,the method comprising:

(a) providing an insect feeding chamber having egg-laying insectspresent therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) introducing said enhanced feedstock into said insect feeding chamberto feed the egg-laying insects present therein;

(d) removing at least a portion of eggs laid by the egg-laying insects;

(e) incubating at least a portion of the removed eggs;

(f) hatching at least a portion of incubated eggs;

(g) introducing a portion of hatched insects into said insect feedingchamber;

(h) removing a portion of said egg-laying insects from said insectfeeding chamber;

(i) grinding a portion of the removed insects to form a stream of groundinsects;

(j) creation of a multifunctional composition by mixing ground insectsof step (i) with one or more ingredients from the group consisting offiber-starch materials, binding agents, density improving texturalsupplements, moisture improving textural supplements, and cannabisenhancers.

FIG. 47:

FIG. 47 shows one non-limiting embodiment of a method for raisingOrthoptera order of insects for the separation of lipids containedwithin said insects. In embodiments, the present disclosure describes amethod for raising Orthoptera order of insects to extract lipidscontained within said insects, the method comprising:

(a) providing an insect feeding chamber having egg-laying insectspresent therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) introducing said enhanced feedstock into said insect feeding chamberto feed the egg-laying insects present therein;

(d) removing at least a portion of eggs laid by the egg-laying insects;

(e) incubating at least a portion of the removed eggs;

(f) hatching at least a portion of incubated eggs;

(g) introducing a portion of hatched insects into said insect feedingchamber;

(h) removing a portion of said egg-laying insects from said insectfeeding chamber;

(i) extracting lipids from a portion of the removed insects.

FIG. 48:

FIG. 48 shows one non-limiting embodiment of another method for raisingOrthoptera order of insects for the extraction of lipids. Inembodiments, the present disclosure describes a method for raisingOrthoptera order of insects to generate a multifunctional composition,the method comprising:

(a) providing a plurality of insect feeding chambers having egg-layinginsects present therein;

(b) mixing feedstock with one or more additives from the groupconsisting of water, minerals, vitamins, and polymer to form an enhancedfeedstock;

(c) apportioning said enhanced feedstock into a plurality of enhancedfeedstock streams; introducing said plurality of enhanced feedstockstreams into said plurality of insect feeding chambers to feed theegg-laying insects present therein;

(d) removing at least a portion of eggs laid by the egg-laying insects;

(e) incubating at least a portion of the removed eggs;

(f) hatching at least a portion of incubated eggs;

(g) introducing a portion of hatched insects into at least one of theplurality of insect feeding chambers;

(h) removing a portion of said egg-laying insects from said plurality ofinsect feeding chambers;

(i) extracting lipids from a portion of the removed insects.

Volume II: Farming Superstructure System (IPSS), Description of theDrawings

The accompanying figures show schematic process flowcharts of preferredembodiments and variations thereof. A full and enabling disclosure ofthe content of the accompanying claims, including the best mode thereofto one of ordinary skill in the art, is set forth more particularly inthe remainder of the specification, including reference to theaccompanying figures showing how the preferred embodiments and othernon-limiting variations of other embodiments described herein may becarried out in practice, in which:

FIG. 1A′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) including a first water treatment unit (A1*), a secondwater treatment unit (A2*), a third water treatment unit (A3*), a commonreservoir (500*), a pump (P1*), a plurality of vertically stackedgrowing assemblies (100*, 200*), a fabric (104*, 204*) that partitionseach growing assembly (100*, 200*) into an upper-section (105*, 205*)and a lower-section (106*, 206*), a plurality of lights (L1*, L2*)positioned within the upper-section (105*, 205*) of each growingassembly.

FIG. 1B′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) that includes a first growing assembly (100*) having afirst growing medium (GM1*) and a second growing assembly (200*) havinga second growing medium (GM2*).

FIG. 1C′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) that includes a first growing assembly (100*) having afirst growing medium (GM1*) and a second growing assembly (200*) havinga second growing medium (GM2*) and the first growing assembly (100*) andsecond growing assembly (200*) are grown outdoors.

FIG. 1D′ depicts one non-limiting embodiment general arrangement of afarming superstructure system (FSS) top-view that includes a firstgrowing assembly (100*) and a second growing assembly (200*) eachconfigured to grow plants (107*, 107A*, 107B*, 107C*, 20*7, 207A*,207B*, 207C*).

FIG. 2′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) including a first vertically stacked system (1500*)including a plurality of vertically stacked growing assemblies (100*,200*) integrated with a first and second vertical support structure(VSS1*, VSS2*) wherein the first growing assembly (100*) is supported bya first horizontal support structure (SS1*) and a second growingassembly (200*) is supported by a second horizontal support structure(SS2*).

FIG. 3′ depicts one non-limiting embodiment of a plurality of verticallystacked systems (1500*, 1500′*) including a first vertically stackedsystem (1500*) and a second vertically stacked system (1500′*), thefirst vertically stacked system (1500*) as depicted in FIG. 2′, alsoboth vertically stacked systems (1500*, 1500′*) are contained within anenclosure (ENC*) having an interior (ENC1*).

FIG. 4A′ depicts one non-limiting embodiment of FIG. 3′ wherein theenclosure (ENC*) is provided with a temperature control unit (TCU*)including an air heat exchanger (HXA*) that is configured to provide atemperature and/or humidity controlled air supply (Q3*) to the interior(ENC1*) of the enclosure (ENC*) which contains a plurality of verticallystacked systems (1500*, 1500′*).

FIG. 4B′ depicts one non-limiting embodiment of FIG. 1B′ and FIG. 4A′wherein the enclosure (ENC*) is provided with a temperature control unit(TCU*) including an air heat exchanger (HXA*) that is configured toprovide a temperature and/or humidity controlled air supply (Q3*) to theinterior (ENC1*) of the enclosure (ENC*) which contains a plurality ofgrowing assemblies (100*, 200*).

FIG. 5A′ depicts one non-limiting embodiment of FIG. 4A′ wherein thetemperature control unit (TCU*) of FIG. 4A′ is contained within theinterior (ENC1*) of the enclosure (ENC*) and coupled with a humiditycontrol unit (HCU*).

FIG. 5B′ depicts one non-limiting embodiment of FIG. 4B′ and FIG. 5A′wherein the temperature control unit (TCU*) of FIG. 4B′ is containedwithin the interior (ENC1*) of the enclosure (ENC*) and coupled with ahumidity control unit (HCU*).

FIG. 5C′ shows one non-limiting embodiment where the compressor (Q30*)within the humidity control unit (HCU*) is that of a thermal compressor(Q30*) that accepts a source of steam.

FIG. 5D′ shows one non-limiting embodiment where the compressor (Q30*)within the humidity control unit (HCU*) is that of a thermal compressor(Q30*) that accepts a source of steam.

FIG. 5E′ elaborates upon FIG. 5D′ and shows one non-limiting embodimentwhere the compressor (Q30*) within the humidity control unit (HCU*) isthat of a thermal compressor (Q30*) that accepts a source of heat, suchas flue gas (FG1*)

FIG. 6′ shows a front view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

FIG. 7′ shows a top view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

FIG. 8′ shows a first side view of one embodiment of a plant growingmodule (PGM*).

FIG. 9′ shows a front view of one embodiment of a liquid distributionmodule (LDM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications andthat is configured to provide a source of liquid to a plurality of plantgrowing modules (PGM*).

FIG. 10′ shows a top view of one embodiment of a liquid distributionmodule (LDM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications andthat is configured to provide a source of liquid to a plurality of plantgrowing modules (PGM*).

FIG. 11′ shows a first side view of one embodiment of a liquiddistribution module (LDM*).

FIG. 12′ shows one non-limiting embodiment of a fabric (104*) used in agrowing assembly (100), the fabric (104) having a multi-pointtemperature sensor (MPT10*0) connected thereto for measuringtemperatures at various lengths along the sensor's length.

FIG. 13′ shows another one non-limiting embodiment of a fabric (104*)used in a growing assembly (100).

FIG. 14′ depicts a computer (COMP) that is configured to input andoutput signals listed in FIGS. 1-17K′.

FIG. 15′ shows a plurality of cannabis trimmers (TR*, TR**) that areconfigured to trim at least a portion of the cannabis (107*, 207*) thatwas growing in each growing assembly (100*, 200*).

FIG. 16′ shows a grinder (GR*) that is configured to grind at least aportion of cannabis plants (107, 207*) that was growing in each growingassembly (100*, 200*).

FIG. 17′ shows a heater (HTR1*) that is configured to heat at least aportion of cannabis plants (107*, 207*) that was growing in each growingassembly (100*, 200*).

FIG. 17A′ shows one non-limiting embodiment of a volatiles extractionsystem (VES*) that is configured to extract volatiles from cannabis(107*, 207*) with a first solvent (SOLV1*).

FIG. 17A″ shows one non-limiting embodiment of a volatiles extractionsystem (VES*) that is configured to extract volatiles from cannabis(107*, 207*) with a chilled ethanol separation system (CESS).

FIG. 17B′ shows a plurality of volatiles extraction systems (VES1*,VES2*) equipped with one first solvent separation system (SSS*).

FIG. 17C′ shows a volatiles and solvent mixing system (VSMS*) that isconfigured to mix the volatiles (VOLT*) with a second solvent (SOLV2*).

FIG. 17D′ shows a separation system (SEPSOL*) that is configured toseparate at least a portion of the solvent (SOLV2*) and/or volatilesand/or cannabinoids from the volatiles and solvent mixture (SVSM*) toproduce concentrated volatiles (CVOLT*).

FIG. 17D″ shows a plurality of sequential separation systems (SEPSOL*,SEPSOL**, SEPSOL***) that are configured to separate at least a portionof the solvent, volatiles, and/or cannabinoids from produce concentratedvolatiles (CVOLT*) and a plurality of different compounds (1SCM*,1SCM**, 2SCM*, 2SCM**)

FIG. 17E′ shows one non-limiting embodiment of a solvent separationsystem that is configured to evaporator the second solvent from thevolatiles and solvent mixture (SVSM*) by use of a spray dryer (KAP*).

FIG. 17E-1′ shows one non-limiting embodiment of a co-current type ofspray dryer (KAP*) that may be used with the solvent separation systemdescribed in FIG. 17E′.

FIG. 17E-2′ shows one non-limiting embodiment of a counter-current typeof spray dryer (KAP*) that may be used with the solvent separationsystem described in FIG. 17E′.

FIG. 17E-3′ shows another non-limiting embodiment of a counter-currenttype of spray dryer (KAP*) that may be used with the solvent separationsystem described in FIG. 17E′.

FIG. 17E-4′ shows one non-limiting embodiment of a mixed-flow type ofspray dryer (KAP*) that may be used with the solvent separation systemdescribed in FIG. 17E′.

FIG. 17F′ shows a power production system (PPS*) that is configured togenerate electricity, heat, or steam for use in the farmingsuperstructure system (FSS).

FIG. 17G′ shows one non-limiting embodiment of a carbon dioxide removalsystem (GAE*) that is configured to remove carbon dioxide from flue gas(LFP*) for use as a source of carbon dioxide (CO2*) in the farmingsuperstructure system (FSS).

FIG. 17H′ shows a cannabinoid extraction system including vessels,filters, pumps, piping connecting flow between vessels and adsorbers,valving, controllers, pressure regulators, metering equipment, flowcontrol, and microprocessor equipment, their construction,implementation, and functionality.

FIG. 17J′ shows one non-limiting embodiment of a cannabinoid emulsionmixing system (17J*).

FIG. 17K′ shows one non-limiting embodiment of a cannabinoid softgelencapsulation system (17K*).

FIG. 18′ shows a simplistic diagram illustrating a multifunctionalcomposition mixing module that is configured to generate amultifunctional composition from at least a portion of Cannabis plants(107*, 207*) that was harvested from each growing assembly (100*, 200*).

FIG. 19′ illustrates a single fully-grown DANLEO III plant.

FIG. 20′ illustrates zoomed-in view of a budding or flowering plant.

FIG. 21′ illustrates a single leaf of DANLEO III.

FIG. 22′ illustrates a trimmed and dried bud (reproductive structure) ofDANLEO III.

FIG. 23′ shows a cannabis cloning assembly (CA*) that is configured toclone cannabis plants and/or DANLEO III (107*, 207*) that were growingin each growing assembly (100*, 200*).

DETAILED DESCRIPTION

Reference will now be made in detail to various embodiments of thedisclosure. Each embodiment is provided by way of explanation of thedisclosure, not limitation of the disclosure. In fact, it will beapparent to those skilled in the art that modifications and variationscan be made in the disclosure without departing from the teaching andscope thereof. For instance, features illustrated or described as partof one embodiment to yield a still further embodiment derived from theteaching of the disclosure. Thus, it is intended that the disclosure orcontent of the claims cover such derivative modifications and variationsto come within the scope of the disclosure or claimed embodimentsdescribed herein and their equivalents.

Additional objects and advantages of the disclosure will be set forth inpart in the description which follows, and in part will be obvious fromthe description, or may be learned by practice of the claims. Theobjects and advantages of the disclosure will be attained by means ofthe instrumentalities and combinations and variations particularlypointed out in the appended claims.

In embodiments, cannabis is grown within the insect productionsuperstructure system (IPSS) as depicted in Volume I. In embodiments,farming superstructure system (FSS) as depicted in Volume II issimultaneously includes the insect production superstructure system(IPSS) as depicted in Volume I. In embodiments, insects are used withinthe farming superstructure system (FSS) to benefit the cannabis plantstherein. In embodiments, insects are used within the farmingsuperstructure system (FSS) to benefit the cannabis plants thereinbecause some omnivorous or carnivorous insects eat insects that wouldotherwise harm the cannabis plants in turn protecting them. Inembodiments, insects are used within the farming superstructure system(FSS) to benefit the cannabis plants therein and to avoid use ofpesticides. In embodiments, any types of plants may be grown within thefarming superstructure system (FSS). In embodiments, any types of plantsmay be grown within the insect production superstructure system (IPSS).

FIG. 1A′

FIG. 1A′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) including a first water treatment unit (A1*), a secondwater treatment unit (A2*), a third water treatment unit (A3*), a commonreservoir (500*), a pump (P1*), a plurality of vertically stackedgrowing assemblies (100*, 200*), a fabric (104*, 204*) that partitionseach growing assembly (100*, 200*) into an upper-section (105*, 205*)and a lower-section (106*, 206*), a plurality of lights (L1*, L2*)positioned within the upper-section (105*, 205*) of each growingassembly, a carbon dioxide tank (CO2T*), a plurality of fans (FN1*,FN2*), a plurality of liquid supply conduits (113*, 213*), a liquidsupply header (300*), at least one filter (F1*, F2*), a plurality ofvalves (V1*, V3*, V4*), a drain port (110*, 210*), and a computer(COMP).

FIG. 1A′ discloses a farming superstructure system (FSS). The farmingsuperstructure system (FSS) includes a first growing assembly (100*) anda second growing assembly (200*) in fluid communication with a commonreservoir (500*). The common reservoir (500*) is provided with a watersupply (01*) via a water supply conduit (02*) and a first water inlet(03*). A plurality of water treatment units (A1*, A2*, A3*), along witha contaminant depleted water valve (V0A*), and a water heat exchanger(HX1*) may be installed on the water supply conduit (02*).

A first water treatment unit (A1*) may be installed on the water supplyconduit (02*). The first water treatment unit (A1*) has a first input(04*) and a first output (05*). A water supply (01*) may be provided tothe first water treatment unit (A1*) via a first input (04*).Contaminants may be removed by the first water treatment unit (A1*) toproduce a first contaminant depleted water (06*) that is discharged viaa first output (05*). In embodiments, the first water treatment unit(A1*) includes a cation and is configured to remove positively chargedions from water to form a positively charged ion depleted water (06A*).The positively charged ions may include of one or more from the groupconsisting of calcium, magnesium, sodium, and iron. In embodiments, thepositively charged ions are comprised of one or more from the groupconsisting of calcium, magnesium, sodium, and iron. In embodiments, thepositively charged ions are comprised of one or more from the groupconsisting of aluminum, barium, beryllium, calcium, chromium(III),copper(I), copper(II), hydrogen, iron(II), iron(III), lead(II),lead(IV), lithium, magnesium, manganese(II), mercury(II), potassium,silver, sodium, strontium, tin(II), tin(IV), and zinc.

In embodiments, the first contaminant depleted water (06*) may be apositively charged ion depleted water (06A*). In embodiments, the firstwater treatment unit (A1*) may include a cation, an anion, a membrane,filter, activated carbon, adsorbent, or absorbent. In embodiments, anactivated carbon bed may be used to remove chlorine from the water.

A second water treatment unit (A2*) may be installed on the water supplyconduit (02*) after the first water treatment unit (A1*). The secondwater treatment unit (A2*) may include a second input (07*) and a secondoutput (08*). The first contaminant depleted water (06*) may be providedto the second water treatment unit (A2*) via a second input (07*). Thefirst contaminant depleted water (06*) may be provided to the secondwater treatment unit (A2*) from the first output (05*) of the firstwater treatment unit (A1*). In embodiments, the positively charged iondepleted water (06A*) may be provided to the second water treatment unit(A2*) via a second input (07*). Contaminants may be removed by thesecond water treatment unit (A2*) to produce a second contaminantdepleted water (09*) that is discharged via a second output (08*). Inembodiments, the second water treatment unit (A2*) includes an anionthat is configured to remove negatively charged ions from the positivelycharged ion depleted water (06A*) to form a negatively charged iondepleted water (09A*). The negatively charged ions may include one ormore from the group consisting of iodine, chloride, and sulfate. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of iodine, chloride, and sulfate. Inembodiments, the negatively charged ions are comprised of one or morefrom the group consisting of acetate, aluminum silicate, anions fromorganic acids, azide, bromide, carbonate, chlorate, chloride, chromate,cyanide, dichromate, dihydrogen phosphate, fluoride, formate, hydride,hydrogen carbonate, hydrogen sulfate, hydrogen sulfite, hydroxide,hypochlorite, iodide, metasilicate, monohydrogen phosphate, nitrate,nitride, nitrite, oxalate, oxide, perchlorate, permanganate, peroxide,phosphate, silicate, sulfate, sulfide, sulfite, superoxide, andthiosulfate.

In embodiments, the second contaminant depleted water (09*) may be anegatively charged ion depleted water (09A*). In embodiments, the secondwater treatment unit (A2*) may include a cation, an anion, a membrane,filter, activated carbon, adsorbent, or absorbent.

A third water treatment unit (A3*) may be installed on the water supplyconduit (02*) after the second water treatment unit (A2*). The thirdwater treatment unit (A3*) may include a third input (10*) and a thirdoutput (11*). The second contaminant depleted water (09*) may beprovided to the third water treatment unit (A3*) via a third input(I0*). The second contaminant depleted water (09*) may be provided tothe third water treatment unit (A3*) from the second output (08*) of thesecond water treatment unit (A2*). In embodiments, the negativelycharged ion depleted water (09A*) may be provided to the third watertreatment unit (A3*) via a third input (10*). Contaminants may beremoved by the third water treatment unit (A3*) to produce a thirdcontaminant depleted water (12*) that is discharged via a third output(I1*). In embodiments, the third water treatment unit (A3*) includes amembrane that is configured to remove undesirable compounds from thenegatively charged ion depleted water (09A*) to form an undesirablecompound depleted water (12A*). The “undesirable compounds” may includeone or more from the group consisting of dissolved organic chemicals,viruses, bacteria, and particulates. In embodiments, the thirdcontaminant depleted water (12*) may be an undesirable compound depletedwater (12A*). In embodiments, the third water treatment unit (A3*) mayinclude a cation, an anion, a membrane, filter, activated carbon,adsorbent, or absorbent. In embodiments, the (10*) the undesirablecompounds depleted water (12A*) has an electrical conductivity rangingfrom 0.10 microsiemens per centimeter to 100 microsiemens percentimeter.

In embodiments, the first water treatment unit (A1*) containing a cationmay be a disposable cartridge, portable tank, cylindrical vessel,automatic unit, or a continuous unit. In embodiments, the second watertreatment unit (A2*) containing an anion may be a disposable cartridge,portable tank, cylindrical vessel, automatic unit, or a continuous unit.In embodiments, the third water treatment unit (A3*) containing amembrane may have: a diameter that ranges from 1 inch to 6 inches; and apore size ranging from 0.0001 microns to 0.5 microns.

The common reservoir (500*) is configured to accept a portion of acontaminant depleted water (06A*, 09A*, 12A*) from the at least onewater treatment unit (A1*, A2*, A3*). In embodiments, the watertreatment units (A1*, A2*, A3*) may be configured to remove solids fromthe water supply (01*). In embodiments, a contaminant depleted watervalve (V0A*) is installed on the water supply conduit (02*) to regulatethe amount of water transferred to the common reservoir (500*) throughthe water supply conduit (02*) and first water inlet (03*). Thecontaminant depleted water valve (V0A*) is equipped with a controller(CVOA*) which sends a signal (XVOA*) to and from a computer (COMP). Inembodiments, a water heat exchanger (HX1*) is installed on the watersupply conduit (02*) to control the temperature of the water transferredto the common reservoir (500*) through the water supply conduit (02*)and first water inlet (03*). In embodiments, the water heat exchanger(HX1*) increases the temperature of the water supply (01*) introduced tothe common reservoir (500*). In embodiments, the water heat exchanger(HX1*) decreases the temperature of the water supply (01*) introduced tothe common reservoir (500*). In embodiments, the water heat exchanger(HX1*) is positioned in between the contaminant depleted water valve(V0A*) and the water inlet (03*) of the common reservoir (500*). So, itis shown that water may be treated with a plurality of water treatmentunits (A1*, A2*, A3*) before being introduced to the common reservoir(500*).

In embodiments, the common reservoir (500) is comprised of metal,plastic, fiberglass, composite materials, or combinations thereof, orany other conceivable material that may contain a liquid within itsinterior. In embodiments, fish (FISH) are contained within the interiorof the common reservoir (500). The fish (FISH) increase theconcentration of nitrogen within the liquid contained within the commonreservoir (500) which in turn can be provided to the cannabis (107,207).

In embodiments, the fish (FISH) excrete nitrogen. In embodiments, thenitrogen excreted from the fish (FISH) includes ammonia or urea. Inembodiments, the nitrogen excreted by the fish (FISH) is consumed by thecannabis (107, 207). In embodiments, the nitrogen excreted by the fish(FISH) is mixed with at least a portion of the first contaminantdepleted water (06), second contaminant depleted water (09), and/orthird contaminant depleted water (12), then pressured and provided tothe cannabis (107, 207). In embodiments, the fish (FISH) are fed insectsfrom the IPSS and/or FSS. In embodiments, the fish (FISH) are used asthe growing medium for the cannabis plants to grow into. In embodiments,the fish (FISH) are used mixed with the insects to provide a source offish protein, fish scales, and or fish meal used in the enhancedfeedstock and/or pet food to feed pets. In embodiments, the fish (FISH)include: bass, carp, catfish, coy, goldfish, perch, salmon, stripedbass, tilapia, trout, and combinations thereof.

In embodiments, the fish (FISH) include: Abramis brama, Acanthopagrusschlegeli, Acipenser baeri, Acipenser ruthenus, Acipenser stellatus,Acipenser transmontanus, Aequidens rivulatus, Anabas testudineus,Anguilla anguilla, Anguilla japonica, Anguilla rostrata, Arapaima gigas,Aspius aspius, Bidyanus bidyanus, Brycon moorei, Carassius auratus,Carassius carassius, Catla catla, Centropomus undecimalis, Channa argus,Channa micropeltes, Channa punctatus, Channa striata, Chanos chanos,Chrysichthys nigrodigitatus, Cichlasoma maculicauda, Cichlasomamanaguense, Cichlasoma urophthalmus, Cirrhinus molitorella, Cirrhinusmrigala, Clarias anguillaris, Clarias batrachus, Clarias fuscus, Clariasgariepinus, Clarias macrocephalus, Colossoma macropomum, Coregonusalbula, Coregonus lavaretus, Ctenopharyngodon idellus, Cyprinus carpio,Dicentrarchus labrax, Diplodus sargus, Dormitator latifrons, Epinephelusakaara, Epinephelus areolatus, Epinephelus tauvina, Esox lucius,Etroplus suratensis, Evynnis japonica, Gadus morhua, Helostomatemmincki, Heterobranchus bidorsalis, Heterobranchus longifilis,Heterotis niloticus, Hoplosternum littorale, Huso huso,Hypophthalmichthys molitrix, Hypophthalmichthys nobilis, Ichthyoelephashumeralis, Ictalurus melas, Ictalurus punctatus, Ictiobus cyprinellus,Labeo calbasu, Labeo rohita, Lates calcarifer, Lates niloticus,Leptobarbus hoeveni, Liza aurata, Liza macrolepis, Liza parsia, Lizaramada, Liza saliens, Liza tade, Lutjanus argentimaculatus,Maccullochella peeli, Macquaria ambigua, Megalobrama amblycephala,Micropterus salmoides, Misgurnus anguillicaudatus, Monopterus albus,Morone saxatilis, Mugil cephalus, Mugil curema, Mugil liza,Mylopharyngodon piceus, Notemigonus crysoleucas, Ocyurus chrysurus,Odontesthes bonariensis, Oncorhynchus gorbuscha, Oncorhynchus keta,Oncorhynchus kisutch, Oncorhynchus masou, Oncorhynchus mykiss,Oncorhynchus nerka, Oncorhynchus tshawytscha, Oreochromis andersonii,Oreochromis aureus, Oreochromis macrochir, Oreochromis mossambicus,Oreochromis niloticus, Oreochromis spilurus, Oreochromis urolepis,Osphronemus goramy, Osteochilus hasselti, Oxyeleotris marmorata, Pagrusmajor, Pagrus pagrus, Pangasius pangasius, Pangasius sutchi, Parabramispekinensis, Paralichthys olivaceus, Perca fluviatilis, Piaractusbrachypomus, Piaractus mesopotamicus, Plecoglossus altivelis,Plectropomus maculatus, Pomatomus saltatrix, Prochilodus reticulatus,Psetta maxima, Puntius gonionotus, Puntius javanicus, Rhabdosargussarba, Rhamdia sapo, Rutilus rutilus, Salmo salar, Salmo trutta,Salvelinus alpinus, Salvelinus fontinalis, Salvelinus namaycush,Sarotherodon melanotheron, Sciaenops ocellatus, Seriola dumerili,Seriola quinqueradiata, Siganus canaliculatus, Siganus guttatus, Siganusrivulatus, Siluris glanis, Solea vulgaris, Sparus aurata, Stizostedionlucioperca, Thunnus maccoyii, Thunnus thynnus, Tilapia guineensis,Tilapia rendalli, Tilapia zillii, Tinca tinca, Trachinotus blochii,Trachinotus carolinus, Trachinotus goodei, Trachurus japonicus,Trichogaster pectoralis, and combinations thereof.

In embodiments, the fish (FISH) include crustaceans, mollusks, aquaticplants, algae, and other organisms. In embodiments, the fish (FISH)include shrimp, mussels, crawfish, clams, and baitfish. In embodiments,the algae include one or more selected from the group consisting of:microalgae, phytoplankton, microphytes, and planktonic algae. Inembodiments, the aquatic plants include seaweed. In embodiments, thealgae include one or more selected from the group consisting of:microalgae, phytoplankton, microphytes, and planktonic algae. Inembodiments, the seaweed includes kelp, Saccharina japonica, Undariapinnatifida, Pyropia spp., Porphyra spp., Pyropia, Porphyra, Kappaphycusalvarezii, Eucheuma striatum, carrageenophytes, Gracilaria,Gracilariopsis spp., agarophytes, and combinations thereof. Inembodiments, the mollusks include fresh water molloscs. In embodiments,the fish (FISH) include freshwater fish. In embodiments, the fish (FISH)include brackish water fish. In embodiments, the fish (FISH) includesaltwater water fish wherein the nitrogen is separated within aseparator and provided to the cannabis plants, insects, and/orpsilocybin mushrooms. In embodiments, the fish (FISH) include eels. Inembodiments, the eels include mollusks attached thereto. In embodiments,the eels include algae attached thereto. In embodiments, mollusks arecomprised of an invertebrate of a large phylum which includes snails,slugs, mussels, clams, and octopuses. They have a soft unsegmented bodyand live in aquatic or damp habitats, and most kinds have an externalcalcareous shell. In embodiments, the preferred type of mollusks to livewithin the common reservoir are freshwater mussels. In embodiments, thepreferred type of mollusks to live within the common reservoir arefreshwater snails. In embodiments, the preferred type of mollusks tolive within the common reservoir are freshwater clams. In embodiments,the preferred type of freshwater mussels include freshwater bivalves. Inembodiments, the preferred type of freshwater mussels include OrderUnionida. In embodiments, the preferred type of freshwater musselsinclude mussels from the family unionidae, etheriidae, hyriidae,iridinidae, margaritiferidae, mutelidae, mycetopodidae, and combinationsthereof. In embodiments, the preferred type of freshwater musselsinclude mother-of-pearl. In embodiments, the freshwater mussels feed onalgae within the common reservoir and filter the water. In embodiments,the freshwater mussels include Elliptio complanata (Eastern elliptio) orStrophitus undulatus (Creeper). In embodiments, the freshwater musselsinclude etheriidae, hyriidae, iridinidae, margaritiferidae, mutelidae,mycetopodidae, or unionidae.

In embodiments, the mosquitos include genetically modified mosquitos. Inembodiments, the mosquitos include Aedes aegypti mosquitoes. Inembodiments, the genetically modified mosquitos include Aedes aegyptimosquitoes. In embodiments, the mosquitos include genetically modifiedmosquitos to assist in insect control and prevent the spread diseaseslike Zika and dengue fever. In embodiments, the mosquitos include anaturally-occurring bacteria called Wolbachia which makes them unable tohave offspring with wild female mosquitoes. In embodiments, Wolbachia isa genus of gram-negative bacteria that infects arthropod species,including a high proportion of insects, and also some nematodes.

For example, the genetically modified mosquitos include may includeOxitec created genetically altered males of the species (OX513A) thatproduce the protein tTA, which negatively affects cell development. Thetransgenic animals need the antibiotic tetracycline to survive. If theseanimals are released in large numbers and mate with females, antibioticdependence is passed to the next generation and the offspring die. Thus,the Aedes aegypti population is greatly reduced and thereby the risk forthe people in that region of contracting a mosquito-born disease. Inembodiments, the genetically modified mosquitos include Asian tigermosquito Aedes albopictus. In embodiments, the insects are geneticallymodified. In embodiments, the insects are transgenic animals. Inembodiments, the predatory mites are transgenic animals. In embodiments,the bats are transgenic animals. In embodiments, the insects aregenetically modified organisms (transgenic organisms). In embodiments,the genetically modified organisms are used as a method of biologicalinsect control (a sterile insect technique) whereby overwhelming numbersof sterile insects are released into the wild. The released insects arepreferably male, as this is more cost-effective and the females may insome situations cause damage by laying eggs in the crop, or, in the caseof mosquitoes, taking blood from humans. The sterile males compete withwild males to mate with the females. Females that mate with a sterilemale produce no offspring, thus reducing the next generation'spopulation. Sterile insects are not self-replicating and, therefore,cannot become established in the environment. Repeated release ofsterile males over low population densities can further reduce and incases of isolation eliminate pest populations, although cost-effectivecontrol with dense target populations is subjected to populationsuppression prior to the release of the sterile males.

In embodiments, the common reservoir (500*) is comprised of metal,plastic, fiberglass, composite materials, or combinations thereof, orany other conceivable material that may contain a liquid within itsinterior. In embodiments, the common reservoir (500*) is configured toaccept a water supply (01*) from the water supply conduit (02*). Inembodiments, the common reservoir (500*) may be configured to accept anypermutation or combination of a water supply (01*) either a firstcontaminant depleted water (06*), second contaminant depleted water(09*), or third contaminant depleted water (12*), that is heated orcooled or not heated or cooled. In embodiments, the common reservoir(500*) may be configured to accept any permutation or combination of awater supply (01*) either a positively charged ion depleted water(06A*), negatively charged ion depleted water (09A*), or undesirablecompounds depleted water (12A*) that is heated or cooled or not heatedor cooled. In embodiments, the common reservoir (500*) may be configuredto accept any permutation or combination of a water supply (01*) fromany number of water treatment units (A1*, A2*, A3*) that includes atleast a cation, an anion, a membrane, a filter, activated carbon,adsorbent, or absorbent.

In embodiments, the common reservoir (500*) is equipped with an upperlevel switch (LH*) for detecting a high level and a lower level switch(LL*) for detecting a lower level. The upper level switch (LH*) isconfigured to output a signal (XLH*) to the computer (COMP*) when theupper level switch (LH*) is triggered by a high level of liquid withinthe common reservoir (500*). The lower level switch (LL*) is configuredto output a signal (XLL*) to the computer (COMP) when the lower levelswitch (LL*) is triggered by a low level of liquid within the commonreservoir (500*). In embodiments, when the lower level switch (LL*)sends a signal (XLL*) to the computer (COMP), the contaminant depletedwater valve (V0A*) is opened and introduces water into the commonreservoir (500*) until the upper level switch (LH*) is triggered thussending a signal (XLH*) to the computer (COMP) to close the contaminantdepleted water valve (V0A*). This level control loop including the upperlevel switch (LH*) for detecting a high level and a lower level switch(LL*) for detecting a lower level may be coupled to the operation of thecontaminant depleted water valve (V0A*) for introducing a water supply(01*) through the water supply conduit (02*) and into the commonreservoir (500*) via the first water inlet (03*).

In embodiments, a pump (P1*) is configured to accept, pressurize, andtransfer liquid within the common reservoir (500*) into a plurality ofvertically stacked growing assemblies (100*, 200*). In embodiments, thepump (P1*) is configured to accept, pressurize, and transfer at least aportion of the undesirable compounds depleted water (12A*) transferredfrom the common tank (500T*) into a plurality of vertically stackedgrowing assemblies (100*, 200*). Each of the plurality of verticallystacked growing assemblies (100*, 200*) are positioned above the commonreservoir (500*).

The first growing assembly (100*) has an interior (I01*), a top (I02*),a bottom (I03*), and a longitudinal axis (AX1*) extending along a heightdirection of the first growing assembly (100*). The first growingassembly (100*) has a fabric (104*) that partitions the first growingassembly (100*) into an upper-section (105*) close to the top (I02*) anda lower-section (106*) close to the bottom (103*). The fabric (104*) isused to provide structure for Cannabis plants (107*) to root into. Forpurposes of simplicity, DANLEO III (107*, 207*) may be referred to andis synonymous with the term cannabis (107*, 207*) for purposes of thisdisclosure. Obviously, the farming systems and methods disclosed hereinpertain to any type plant and even any type of cannabis plant (107*,207*) and not only limited to growing DANLEO III (107*, 207*). GrowingDANLEO III (107*, 207*) within the farming superstructure system (FSS)is merely a non-limiting example of any type of the cannabis (107*,207*) that can be grown within the farming superstructure system (FSS).In fact, any type of plant (107*, 207*) may be grown using the farmingsystems and methods disclosed herein. In embodiments, any types ofplants (107*, 207*) may be grown within the Farming SuperstructureSystem FSS).

Cannabis plants (107*) rooted in the fabric (104*) have roots that growdownward and extend into the lower-section (106*). The first growingassembly (100*) is equipped with a plurality of lights (L1*) positionedwithin the upper-section (105*) above the fabric (104*). Cannabis (107*)rooted in the fabric (104*) grow upward extending into the upper-section(105*) towards the plurality of lights (L1*). The plurality of lights(L1*) are configured to be controlled by a computer (COMP) to operate ata wavelength ranging from 400 nm to 700 nm. In embodiments, the lights(L1*) have a controller (CL1*) that sends a signal (XL1*) to and fromthe computer (COMP). In embodiments, the lights (L1*, L2*) may becompact fluorescent (CFL), light emitting diode (LED), incandescentlights, fluorescent lights, s, metal halide lamps, high-intensitydischarge (HID) gas discharge lamps, low pressure sodium lamps, sodiumlamps, and combinations thereof. In embodiments, light emitting diodesare preferred. In embodiments, low pressure sodium lamps are preferred.In embodiments, the lights provide heat to the cannabis plants. Inembodiments, the lights are turned on and off to provide an illuminationon-off ratio. In embodiments, the cannabis plants are not heated withlights when the lights are off. In embodiments, the cannabis plants areheat with heaters when the lights are off.

In embodiments, a first plurality of lights (L1*) in the first growingassembly (100*) include a first plurality of light emitting diodes(LED*). In embodiments, the first plurality of light emitting diodes(LED*) include blue LEDs (BLED*), red LEDS (RLED*), and/or green LEDS(GLED*). In embodiments, the first plurality of light emitting diodes(LED*) in the first growing assembly (100*) include one or two or morefrom the group consisting of blue LEDs (BLED*), red LEDS (RLED*), andgreen LEDS (GLED*).

In embodiments, a second plurality of lights (L2*) in the second growingassembly (200*) include a second plurality of light emitting diodes(LED′*). In embodiments, the second plurality of light emitting diodes(LED′*) include blue LEDs (BLED′*), red LEDS (RLED′*), and/or green LEDS(GLED′*). In embodiments, the second plurality of light emitting diodes(LED′*) in the second growing assembly (200*) include one or two or morefrom the group consisting of blue LEDs (BLED′*), red LEDS (RLED′*), andgreen LEDS (GLED′*).

In embodiments, the blue LEDs (BLED*, BLED′*) operate at a wavelengththat ranges from 490 nanometers (nm) to 455 nm. In embodiments, the redLEDs (RLED*, RLED′*) operate at a wavelength that ranges from 620 nm to780 nm. In embodiments, the green LEDs (GLED*, GLED′*) operate at awavelength that ranges from 490 nm to 577 nm. In embodiments, theplurality of light emitting diodes (LED) are configured to be controlledby a computer (COMP) to operate at a wavelength ranging from 490 nm to780 nm. In embodiments, the plurality of light emitting diodes (LED) areconfigured to be controlled by a computer (COMP) to operate at awavelength ranging from 400 nm to 700 nm.

In embodiments, the first plurality of light emitting diodes (LED*) andsecond plurality of light emitting diodes (LED″*) are configured tooperate in the following manner:

-   -   (a) illuminating plants with blue LEDs (BLED*, BLED′*) and red        LEDs (RLED, RLED′*); and    -   (b) illuminating the plants nanometers with green LEDs (GLED*,        GLED′*);        wherein:

the blue LEDs (BLED*, BLED′*) operate at a wavelength that ranges from490 nanometers to 455 nanometers;

the red LEDs (RLED*, RLED′*) operate at a wavelength that ranges from620 nanometers to 780 nanometers;

the green LEDs (GLED*, GLED′*) operate at a wavelength that ranges from490 nanometers to 577 nanometers.

In embodiments, the first plurality of light emitting diodes (LED*) andsecond plurality of light emitting diodes (LED*) are configured tooperate in the following manner:

-   -   (a) providing:        -   (a1) a first growing assembly (100*) having a first            plurality of light emitting diodes (LED*), the first            plurality of light emitting diodes (LED*) in the first            growing assembly (100*) include blue LEDs (BLED*), red LEDS            (RLED*), and green LEDS (GLED*);        -   (a2) a second growing assembly (200*) having a second            plurality of light emitting diodes (LED*), the second            plurality of light emitting diodes (LED′*) in the second            growing assembly (200*) include blue LEDs (BLED′*), red LEDS            (RLED′*), and green LEDS (GLED′*);    -   (b) illuminating the interiors of the first growing assembly        (100*) and second growing assembly (200*) with green LEDs        (GLED*, GLED′*) and optionally with blue LEDs (BLED*, BLED′*) or        red LEDs (RLED*, RLED′*); and    -   (c) illuminating the interiors of the first growing assembly        (100*) and second growing assembly (200*) with blue LEDs (BLED*,        BLED′*) and red LEDs (RLED*, RLED′*); and        wherein:

the blue LEDs (BLED*, BLED′*) operate at a wavelength that ranges from490 nanometers to 455 nanometers;

the red LEDs (RLED*, RLED′*) operate at a wavelength that ranges from620 nanometers to 780 nanometers;

the green LEDs (GLED*, GLED′*) operate at a wavelength that ranges from490 nanometers to 577 nanometers.

In embodiments, the disclosure provides for a farming method, including:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first water treatment unit (A1*) including a cation            configured to remove positively charged ions from water to            form a positively charged ion depleted water (06A*), the            positively charged ions are comprised of one or more from            the group consisting of calcium, magnesium, sodium, and            iron;        -   (a2) a second water treatment unit (A2*) including an anion            configured to remove negatively charged ions from the            positively charged ion depleted water (06A*) to form a            negatively charged ion depleted water (09A*), the negatively            charged ions are comprised of one or more from the group            consisting of iodine, chloride, and sulfate;        -   (a3) a first growing assembly (100*) having a first            plurality of light emitting diodes (LED*), the first            plurality of light emitting diodes (LED*) in the first            growing assembly (100*) include blue LEDs (BLED*) and red            LEDS (RLED*), and optionally green LEDS (GLED*);        -   (a4) a second growing assembly (200*) having a second            plurality of light emitting diodes (LED′*), the second            plurality of light emitting diodes (LED′*) in the second            growing assembly (200*) include blue LEDs (BLED′*) and red            LEDS (RLED′*), and optionally green LEDS (GLED′*);    -   (b) providing a source of water;    -   (c) removing positively charged ions from the water of step (b)        to form a positively charged ion depleted water;    -   (d) removing negatively charged ions from the water after        step (c) to form a negatively charged ion depleted water;    -   (e) mixing the negatively charged ion depleted water after        step (d) with one or more from the group consisting of        macro-nutrients, micro-nutrients, and a pH adjustment to form a        liquid mixture;    -   (f) pressurizing the liquid mixture of step (e) to form a        pressurized liquid mixture;    -   (g) splitting the pressurized liquid mixture into a plurality of        pressurized liquid mixtures;    -   (h) transferring the plurality of pressurized liquid mixtures to        each growing assembly;    -   (i) illuminating the interiors of the first growing assembly        (100*) and second growing assembly (200*) with blue LEDs (BLED*,        BLED′*) and red LEDs (RLED*, RLED′*); and    -   (j) optionally illuminating the interiors of the first growing        assembly (100*) and second growing assembly (200*) with green        LEDs (GLED*, GLED′*);        wherein:

the blue LEDs (BLED*, BLED′*) operate at a wavelength that ranges from490 nanometers to 455 nanometers;

the red LEDs (RLED*, RLED′*) operate at a wavelength that ranges from620 nanometers to 780 nanometers;

the green LEDs (GLED*, GLED′*) operate at a wavelength that ranges from490 nanometers to 577 nanometers;

the positively charged ions are comprised of one or more from the groupconsisting of calcium, magnesium, sodium, and iron;

the negatively charged ions are comprised of one or more from the groupconsisting of iodine, chloride, and sulfate;

the macro-nutrients are comprised of one or more from the groupconsisting of nitrogen, phosphorus, potassium, calcium, magnesium, andsulfur;

the micro-nutrients are comprised of one or more from the groupconsisting of iron, manganese, boron, molybdenum, copper, zinc, sodium,chlorine, and silicon;

the pH adjustment solution is comprised of one or more from the groupconsisting acid, nitric acid, phosphoric acid, potassium hydroxide,sulfuric acid, organic acids, citric acid, and acetic acid;

the blue LEDs (BLED*, BLED′*) or red LEDs (RLED*, RLED′*) illuminate theinteriors of the first growing assembly (100*) and second growingassembly (200*) at an illumination on-off ratio ranging from between 0.5and 5, the illumination on-off ratio is defined as the duration of timewhen the lights are on and illuminate in hours divided by the subsequentduration of time when the lights are off and are not illuminating inhours before the lights are turned on again.

In embodiments, the disclosure provides for a farming method, including:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first growing assembly (100*) having a first            plurality of light emitting diodes (LED*), the first            plurality of light emitting diodes (LED*) in the first            growing assembly (100*) blue LEDs (BLED*) and red LEDS            (RLED*), and optionally green LEDS (GLED*);        -   (a2) a second growing assembly (200*) having a second            plurality of light emitting diodes (LED′*), the second            plurality of light emitting diodes (LED′*) in the second            growing assembly (200*) include blue LEDs (BLED′*) and red            LEDS (RLED′*), and optionally green LEDS (GLED′*);    -   (b) illuminating the interiors of the first growing assembly        (100*) and second growing assembly (200*) with blue LEDs (BLED*,        BLED′*) and red LEDs (RLED*, RLED′*); and    -   (c) optionally illuminating the interiors of the first growing        assembly (100*) and second growing assembly (200*) with green        LEDs (GLED*, GLED′*);        wherein:

the blue LEDs (BLED*, BLED′*) operate at a wavelength that ranges from490 nanometers to 455 nanometers;

the red LEDs (RLED*, RLED′*) operate at a wavelength that ranges from620 nanometers to 780 nanometers;

the green LEDs (GLED*, GLED′*) operate at a wavelength that ranges from490 nanometers to 577 nanometers;

the blue LEDs (BLED*, BLED′*) or red LEDs (RLED*, RLED′*) illuminate theinteriors of the first growing assembly (100*) and second growingassembly (200*) at an illumination on-off ratio ranging from between 0.5and 5, the illumination on-off ratio is defined as the duration of timewhen the lights are on and illuminate in hours divided by the subsequentduration of time when the lights are off and are not illuminating inhours before the lights are turned on again.

In embodiments, the disclosure provides for a farming method, including:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first growing assembly (100*) having a first            plurality of light emitting diodes (LED*), the first            plurality of light emitting diodes (LED*) in the first            growing assembly (100*) blue LEDs (BLED*) and red LEDS            (RLED*), and optionally green LEDS (GLED*);        -   (a2) a second growing assembly (200*) having a second            plurality of light emitting diodes (LED′*), the second            plurality of light emitting diodes (LED′*) in the second            growing assembly (200*) include blue LEDs (BLED′*) and red            LEDS (RLED′*), and optionally green LEDS (GLED′*);        -   (a3) a carbon dioxide tank (CO2T*), at least one carbon            dioxide valve (V8*, V9*, V10*), the at least one carbon            dioxide valve (V8*, V9*, V10*) is configured to take a            pressure drop of greater than 50 pounds per square inch,            carbon dioxide is made available to the first growing            assembly (100*) or second growing assembly (200*);    -   (b) illuminating the interiors of the first growing assembly        (100*) and second growing assembly (200*) with blue LEDs (BLED*,        BLED′*) and red LEDs (RLED*, RLED′*); and    -   (c) optionally illuminating the interiors of the first growing        assembly (100*) and second growing assembly (200) with green        LEDs (GLED*, GLED′*);    -   (d) adjusting the carbon dioxide concentration within the first        growing assembly (100*) or second growing assembly (200*) to a        range between 400 parts per million and 10,000 parts per        million;        wherein:

the blue LEDs (BLED*, BLED′*) operate at a wavelength that ranges from490 nanometers to 455 nanometers;

the red LEDs (RLED*, RLED′*) operate at a wavelength that ranges from620 nanometers to 780 nanometers;

the green LEDs (GLED*, GLED′*) operate at a wavelength that ranges from490 nanometers to 577 nanometers;

the blue LEDs (BLED*, BLED′*) or red LEDs (RLED*, RLED′*) illuminate theinteriors of the first growing assembly (100*) and second growingassembly (200*) at an illumination on-off ratio ranging from between 0.5and 5, the illumination on-off ratio is defined as the duration of timewhen the lights are on and illuminate in hours divided by the subsequentduration of time when the lights are off and are not illuminating inhours before the lights are turned on again.

The second growing assembly (200*) has an interior (201*), a top (202*),a bottom (203*), and a longitudinal axis (AX2*) extending along a heightdirection of the first growing assembly (200*). The second growingassembly (200*) has a fabric (204*) that partitions the second growingassembly (200*) into an upper-section (205*) close to the top (202*) anda lower-section (206*) close to the bottom (203*). The fabric (204*) isused to provide structure for cannabis (207*) to root into. Cannabis(207*) rooted in the fabric (204*) have roots that grow downward andextend into the lower-section (206*). The second growing assembly (200*)is equipped with a plurality of lights (L2*) positioned within theupper-section (205*) above the fabric (204*). Cannabis (207*) rooted inthe fabric (204*) grow upward extending into the upper-section (205*)towards the plurality of lights (L2*). The plurality of lights (L2*) areconfigured to be controlled by a computer (COMP*) to operate at awavelength ranging from 400 nm to 700 nm. In embodiments, the lights(L2*) have a controller (CL2*) that sends a signal (XL2*) to and fromthe computer (COMP).

In embodiments, the farming superstructure system (FSS) is equipped witha carbon dioxide tank (CO2T*). The carbon dioxide tank (CO2T*) containspressurized carbon dioxide (CO2*) and is equipped with a carbon dioxidepressure sensor (CO2P*). A carbon dioxide supply header (CO2H*) isconnected to the carbon dioxide tank (CO2T*). A first carbon dioxidesupply valve (V10*) is installed on the carbon dioxide supply header(CO2H*) and is configured to take a pressure drop of greater than 50pounds per square inch (PSI). The first growing assembly (100*) isequipped with a CO2 input (115*) that is connected to a CO2 supplyconduit (116*). The second growing assembly (200*) is also equipped witha CO2 input (215*) that is connected to a CO2 supply conduit (216*).

The CO2 supply conduit (116*) of the first growing assembly (100*) isconnected to the carbon dioxide supply header (CO2H*) via a CO2 headerconnection (115X*). The CO2 supply conduit (116*) of the first growingassembly (100*) is configured to transfer carbon dioxide into the firstinterior (101*) of the first growing assembly (100*). In embodiments, asecond carbon dioxide supply valve (V8*) is installed on the CO2 supplyconduit (116*) of the first growing assembly (100*). The second carbondioxide supply valve (V8*) is equipped with a controller (CV8*) thatsends a signal (XV8*) to and from a computer (COMP). In embodiments, aCO2 flow sensor (FC1*) is installed on the CO2 supply conduit (116*) ofthe first growing assembly (100*). The CO2 flow sensor (FC1*) sends asignal (XFC1*) to the computer (COMP). In embodiments, a gas qualitysensor (GC1*) is installed on the first growing assembly (100*) tomonitor the concentration of carbon dioxide within the first interior(101*). The gas quality sensor (GC1*) is equipped to send a signal(XGC1*) to the computer (COMP).

The CO2 supply conduit (216*) of the second growing assembly (200*) isconnected to the carbon dioxide supply header (CO2H*) via a CO2 headerconnection (215X*). The CO2 supply conduit (216*) of the second growingassembly (200*) is configured to transfer carbon dioxide into the secondinterior (201*) of the second growing assembly (100*). In embodiments, athird carbon dioxide supply valve (V9*) is installed on the CO2 supplyconduit (216*) of the second growing assembly (200*). The third carbondioxide supply valve (V9*) is equipped with a controller (CV9*) thatsends a signal (XV9*) to and from a computer (COMP). In embodiments, aCO2 flow sensor (FC2*) is installed on the CO2 supply conduit (216*) ofthe second growing assembly (200*). The CO2 flow sensor (FC2*) sends asignal (XFC2*) to the computer (COMP). In embodiments, a gas qualitysensor (GC2*) is installed on the second growing assembly (200*) tomonitor the concentration of carbon dioxide within the second interior(201*). The gas quality sensor (GC2*) is equipped to send a signal(XGC2*) to the computer (COMP).

In embodiments, the carbon dioxide concentration in the upper-section(105*, 205*) of each growing assembly ranges from between 400 parts permillion (ppm) to 500 ppm, 500 ppm to 600 ppm, 600 ppm to 700 ppm, 700ppm to 800 ppm, 800 ppm to 900 ppm, 900 ppm to 1000 ppm, 1000 ppm to1500 ppm, 1500 ppm to 2000 ppm, 2000 ppm to 2500 ppm, 2500 ppm to 3000ppm, 3000 ppm to 3500 ppm, 3500 ppm to 4000 ppm, 4000 ppm to 4500 ppm,4500 ppm to 5000 ppm, 5000 ppm to 5500 ppm, 5500 ppm to 6000 ppm, 6000ppm to 6500 ppm, 6500 ppm to 7000 ppm, 7000 ppm to 7500 ppm, 7500 ppm to8000 ppm, 8000 ppm to 8500 ppm, 8500 ppm to 9000 ppm, 9000 ppm to 9500ppm, or 9500 ppm to 10000 ppm.

In embodiments, the gas quality sensor (GC2*) is equipped to send asignal (XGC2*) to the computer (COMP) to operate the first, second, orthird carbon dioxide supply valves (V8*, V9*, V10*).

At least one fan (FN1*) is positioned in the upper-section (105*) of thefirst growing assembly (100*). The fan (FN1*) is configured to blow aironto the cannabis (107*). The fan (FN1*) is configured to distribute amixture of air and CO2 onto the cannabis (107*). The fan (FN1*) isequipped with a controller (CF1*) that sends a signal (XF1*) to and froma computer (COMP).

A plurality of fans (FN2*) are positioned in the upper-section (205*) ofthe second growing assembly (200*). The fans (FN2*) are configured toblow air onto the cannabis (207*). In embodiments, the fans blow air andthe air is comprised of a gas, vapor, and solid particulates. Inembodiments, the gas within air may be oxygen, carbon dioxide, ornitrogen. In embodiments, the vapor within the air may be water vapor.In embodiments, the solid particulates within air may be dust, dirt, orpollen. The fans (FN2*) are configured to distribute a mixture of airand CO2 onto the cannabis (207*). The fans (FN2*) are equipped with acontroller (CF2*) that sends a signal (XF2*) to and from a computer(COMP). Each of the fans (FN1*, FN2*) is configured to operate at a RPMless than 6,000 RPM. In embodiments, it is preferred to operate the fans(FN1*, FN2*) at a RPM less than 6,000 so that the velocity of air blownonto the cannabis ranges from 0.5 feet per second (fps) to 1 fps, 1 fpsto 5 fps, 5 fps to 10 fps, 10 fps to 15 fps, 15 fps to 20 fps, 20 fps to25 fps, 25 fps to 30 fps, 30 fps to 35 fps, 35 fps to 40 fps, 40 fps to45 fps, or 45 fps to 50 fps.

The first growing assembly (100*) is equipped with a temperature sensor(T1*) to monitor the temperature within the first interior (101*). Thetemperature sensor (T1*) is configured to send a signal (XT1*) to thecomputer (COMP). In embodiments, the temperature sensor (T1*) may be amulti-point temperature sensor (MPT100*) that is connected to the fabric(104*) for measuring temperatures at various lengths along the sensor'slength and long the length of the fabric (104*), as depicted in FIGS.12′ and 13′.

The second growing assembly (200*) is equipped with a temperature sensor(T2*) to monitor the temperature within the second interior (201*). Thetemperature sensor (T2*) is configured to send a signal (XT2*) to thecomputer (COMP). In embodiments, the temperature sensor (T2*) may be amulti-point temperature sensor (MPT100*) that is connected to the fabric(204*) for measuring temperatures at various lengths along the sensor'slength and long the length of the fabric (204*), as depicted in FIGS.12′ and 13′.

In embodiments, each growing assembly (100*, 200*) is equipped with anupper temperature sensor (T1C*, T2C*) positioned within theupper-section (105*, 205*), a partition temperature sensor (T1B*, T2B*)positioned at the fabric (104*), and a lower temperature sensor (T1A*,T2A*) positioned within the lower-section (106*, 206*). Preferably thepartition temperature sensor (T1B*) is a multi-point temperature sensor(MPT100*) that is integrated with the fabric (104*) as disclosed inFIGS. 12′ and 13′.

In embodiments, the upper temperature sensor (T1C*, T2C*) is configuredto input a signal (XT1C*, XT2C*) (not shown) to the computer (COMP). Inembodiments, the partition temperature sensor (T1B*, T2B*) is configuredto input a signal (XT1B*, XT2B*) (not shown) to the computer (COMP). Inembodiments, the lower temperature sensor (T1A*, T2B*) is configured toinput a signal (XT1A*, XT2A*) (not shown) to the computer (COMP). Inembodiments, during the day-time, the upper-section (105*, 205*) has atemperature that is greater than the temperature within lower-section(106*, 206*). In embodiments, during the night-time, the upper-section(105*, 205*) has a temperature that is less than the temperature withinthe lower-section (106*, 206*).

A first liquid distributor (108*) is positioned in the lower-section(106*) of the first growing assembly (100*) below the fabric (104*) andequipped with a plurality of restrictions (109*) installed thereon. Inembodiments, the restrictions (109*) of the first liquid distributor(108*) are spray nozzles, spray balls, or apertures. Each restriction(109*) is configured to accept pressurized liquid from the pump (P1*)and introduce the liquid into the lower-section (106*) of the firstgrowing assembly (100*) while reducing the pressure of the liquid thatpasses through each restriction (109*). The first liquid distributor(108*) is connected to a first liquid supply conduit (113*) via a liquidinput (114*). The first liquid distributor (108*) is configured toreceive liquid from a first liquid supply conduit (113*).

A second liquid distributor (208*) is positioned in the lower-section(206*) of the second growing assembly (200*) below the fabric (204*) andequipped with a plurality of restrictions (209*) installed thereon. Inembodiments, the restrictions (209*) of the second liquid distributor(208*) are spray nozzles, spray balls, or apertures. Each restriction(209*) is configured to accept pressurized liquid from the pump (P1*)and introduce the liquid into the lower-section (206*) of the secondgrowing assembly (200*) while reducing the pressure of the liquid thatpasses through each restriction (209*). The second liquid distributor(208*) is connected to a second liquid supply conduit (213*) via aliquid input (214*). The second liquid distributor (208*) is configuredto receive liquid from a second liquid supply conduit (213*).

The first liquid supply conduit (113*) is connected to a liquid supplyheader (300*) via a first connection (X1*). The second liquid supplyconduit (213*) is connected to a liquid supply header (300*) via asecond connection (X2*). The liquid supply header (300*) is connected tothe pump discharge conduit (304*). In embodiments, the liquid supplyheader (300*) has a diameter (D1*) that is greater than both the firstsmaller diameter (D2*) of the first liquid supply conduit (113*) and thesecond smaller diameter (D3*) of the second liquid supply conduit(213*). A first reducer (R1*) may be positioned on the first liquidsupply conduit (113*) in between the first connection (X1*) to theliquid supply header (300*) and the liquid input (I14*) to the firstgrowing assembly (100*). A second reducer (R2*) may be positioned on thesecond liquid supply conduit (213*) in between the second connection(X2*) to the liquid supply header (300*) and the liquid input (214*) tothe second growing assembly (200*).

A first growing assembly liquid supply valve (V3*) may be positioned onthe first liquid supply conduit (113*) in between the liquid supplyheader (300*) and the first growing assembly (100*). The first growingassembly liquid supply valve (V3*) has a controller (CV3*) that isconfigured to input and output a signal (XV3*) to or from the computer(COMP). A second growing assembly liquid supply valve (V4*) may bepositioned on the second liquid supply conduit (213*) in between theliquid supply header (300*) and the second growing assembly (200*). Thesecond growing assembly liquid supply valve (V4*) has a controller(CV4*) that is configured to input and output a signal (XV4*) to or fromthe computer (COMP).

A back-flow prevention valve (BF1*) may be positioned on the firstliquid supply conduit (113*) in between the liquid supply header (300*)and the first growing assembly (100*). FIG. 1A′ shows the back-flowprevention valve (BF1*) positioned in between the first growing assemblyliquid supply valve (V3*) and the first growing assembly (100*). Aback-flow prevention valve (BF2*) may be positioned on the second liquidsupply conduit (213*) in between the liquid supply header (300*) and thesecond growing assembly (200*). FIG. 1A′ shows the back-flow preventionvalve (BF2*) positioned in between the second growing assembly liquidsupply valve (V4*) and the second growing assembly (200*).

A second oxygen emitter (EZ2*) may be positioned on the first liquidsupply conduit (113*) in between the liquid supply header (300*) and thefirst growing assembly (200*). The second oxygen emitter (EZ2*) isconfigured to oxygenate a portion of the liquid that flows through thefirst liquid supply conduit (113*). The second oxygen emitter (EZ2*)inputs signal (XEZ3*) from a computer (COMP). A third oxygen emitter(EZ3*) may be positioned on the second liquid supply conduit (213*) inbetween the liquid supply header (300*) and the second growing assembly(200*). The third oxygen emitter (EZ3*) is configured to oxygenate aportion of the liquid that flows through the second liquid supplyconduit (213*). The third oxygen emitter (EZ3*) inputs signal (XEZ3*)from a computer (COMP).

In embodiments, the oxygen emitter is an electrolytic cell configured toproduce oxygenated water. In embodiments, oxygenated water produced bythe electrolytic cell may have microbubbles and nanobubbles of oxygensuspended within it. In embodiments, the oxygen emitter is anelectrolytic cell which generates microbubbles and nanobubbles of oxygenin a liquid, which bubbles are too small to break the surface tension ofthe liquid, resulting in a liquid that is supersaturated with oxygen.“Supersaturated” means oxygen at a higher concentration than normalcalculated oxygen solubility at a particular temperature and pressure.In embodiments, the very small oxygen bubbles remain suspended in theliquid, forming a solution supersaturated in oxygen. The use ofsupersaturated or oxygenated water for enhancing the growth of cannabismay be incorporated into the FSS. Electrolytic generation ofmicrobubbles or nanobubbles of oxygen for increasing the oxygen contentof flowing liquid may be incorporated into the FSS. In embodiments, theproduction of oxygen and hydrogen by the electrolysis of water may beused to enhance the efficiency of the FSS.

In embodiments, an electrolytic cell is comprised of an anode and acathode. A current is applied across an anode and a cathode of theelectrolytic cell which are immersed in a liquid. Hydrogen gas isproduced at the cathode and oxygen gas is produced at the anode. Inembodiments, the electrolytic cell tends to deactivate and have alimited life if exposed to the positively charged ions, negativelycharged ions, or undesirable compounds. Therefore, a sophisticated watertreatment unit is needed for the electrolytic cell to work properlydeactivate by unpredictable amounts of positively charged ions, removenegatively charged ions, or undesirable components. The roots of thecannabis in the lower section (106*, 206*) are healthier when contactedwith an oxygenated liquid. Further, oxygenated and/or supersaturatedwater inhibits the growth of deleterious fungi on the fabric (104*,204*). In embodiments, the oxygen emitter may be a sparger forincreasing the oxygen content of a liquid by sparging with air oroxygen. In embodiments, the oxygen emitter may be a microbubblegenerator that achieves a bubble size of about 0.10 millimeters to about3 millimeters in diameter. In embodiments, the oxygen emitter may be amicrobubble generator for producing microbubbles, ranging in size from0.1 to 100 microns in diameter, by forcing air into the fluid at highpressure through an orifice.

The common reservoir (500*) is configured to accept a water supply(01*). In embodiments, the common reservoir (500*) is configured toaccept a water supply (01*) that has passed through one or more watertreatment units (A1*, A2*, Δ3*). In embodiments, the common reservoir(500*) is configured to accept a portion of the undesirable compoundsdepleted water (12A*).

The common reservoir (500*) is configured to accept macro-nutrients(601*) from a macro-nutrient supply tank (600*), micro-nutrients (701*)from a micro-nutrient supply tank (700*), and a pH adjustment solution(801*) from a pH adjustment solution supply tank (800*). In embodiments,the macro-nutrients (601*) include one or more from the group consistingof nitrogen, phosphorus, potassium, calcium, magnesium, and sulfur. Inembodiments, the micro-nutrients (701*) include one or more from thegroup consisting of iron, manganese, boron, molybdenum, copper, zinc,sodium, chlorine, and silicon. In embodiments, the pH adjustmentsolution (801*) includes one or more from the group consisting acid,nitric acid, phosphoric acid, potassium hydroxide, sulfuric acid,organic acids, citric acid, and acetic acid.

In embodiments, the macro-nutrient supply tank (600*) is connected tothe common reservoir (500*) via a macro-nutrient transfer conduit (602*)and a macro-nutrient reservoir input (Z1*). A macro-nutrient supplyvalve (V5*) is installed on the macro-nutrient transfer conduit (602*).The macro-nutrient supply valve (V5*) is equipped with a controller(CV5*) that inputs and outputs a signal (XV5*) to and from the computer(COMP). A macro-nutrient flow sensor (F5*) is installed on themacro-nutrient transfer conduit (602*) and configured to output a signal(XF5*) to or from a computer (COMP). Macro-nutrients (601*) may betransferred to the interior of the common reservoir (500*) via amacro-nutrient transfer conduit (602*) by operation with amacro-nutrient supply tank (600*) load cell (604*) to measure theloss-in-mass of the macro-nutrients (601*) within the macro-nutrientsupply tank (600*) or the macro-nutrient transfer conduit (602*).Macro-nutrients (601*) are introduced into the interior of the commonreservoir (500*) beneath the liquid level via a diptube (606*).

In embodiments, the micro-nutrient supply tank (700*) is connected tothe common reservoir (500*) via a micro-nutrient transfer conduit (702*)and a micro-nutrient reservoir input (Z2*). A micro-nutrient supplyvalve (V6*) is installed on the micro-nutrient transfer conduit (702*).The micro-nutrient supply valve (V6*) is equipped with a controller(CV6*) that inputs and outputs a signal (XV6*) to and from the computer(COMP). A micro-nutrient flow sensor (F6*) is installed on themicro-nutrient transfer conduit (702*) and configured to output a signal(XF6*) to or from a computer (COMP). Micro-nutrients (701*) may betransferred to the interior of the common reservoir (500*) via amicro-nutrient transfer conduit (702*) by operation with amicro-nutrient supply tank (700*) load cell (704*) to measure theloss-in-mass of the micro-nutrients (701*) within the micro-nutrientsupply tank (700*) or the micro-nutrient transfer conduit (702*).Macro-nutrients (601*) are introduced into the interior of the commonreservoir (500*) beneath the liquid level via a diptube (606*) (notshown).

In embodiments, the pH adjustment solution supply tank (800*) isconnected to the common reservoir (500*) via a pH adjustment solutiontransfer conduit (802*) and a pH adjustment solution reservoir input(Z3*). A pH adjustment solution supply valve (V8*) is installed on thepH adjustment solution transfer conduit (802*). The pH adjustmentsolution supply valve (V8*) is equipped with a controller (CV8*) thatinputs and outputs a signal (XV8*) to and from the computer (COMP). A pHadjustment solution flow sensor (F7*) is installed on the pH adjustmentsolution transfer conduit (802*) and configured to output a signal(XF7*) to or from a computer (COMP). A pH adjustment solution (801*) maybe transferred to the interior of the common reservoir (500*) via a pHadjustment solution transfer conduit (802*) by operation with a pHadjustment solution supply tank (800*) load cell (804*) to measure theloss-in-mass of the pH adjustment solution (801*) within the pHadjustment solution supply tank (800*) or the pH adjustment solutiontransfer conduit (802*). The pH adjustment solution (801*) areintroduced into the interior of the common reservoir (500*) beneath theliquid level via a diptube (806*) (not shown).

The common reservoir (500*) is configured to accept liquid drained fromeach growing assembly (100*, 200*). The common reservoir (500*) isconfigured to accept liquid drained from the first growing assembly(100*). A drain port (110*) is installed on the lower-section (106*) ofthe first growing assembly (100*) and is configured to drain liquid intoa common reservoir (500*) via a drain conduit (111*). In embodiments,the first growing assembly (100*) is connected to the common reservoir(500*) via a drain conduit (111*). The common reservoir (500*) isconfigured to accept liquid drained from the second growing assembly(200*). A drain port (210*) is installed on the lower-section (206*) ofthe second growing assembly (200*) and is configured to drain liquidinto a common reservoir (500*) via a drain conduit (211*). Inembodiments, the second growing assembly (200*) is connected to thecommon reservoir (500*) via a drain conduit (211*). It is preferable todrain liquid from each growing assembly at a velocity less than 3 feetper second (fps) or 0.25 fps to 0.50 fps, 0.50 fps to 0.75 fps, 0.75 fpsto 1.00 fps, 1.00 fps to 1.25 fps, 1.25 fps to 1.50 fps, 1.50 fps to1.75 fps, 1.75 fps to 2.00 fps, 2.00 fps to 2.25 fps, 2.25 fps to 2.50fps, 2.50 fps to 2.75 fps, 2.75 fps to 3.00 fps, 3.00 fps to 3.25 fps,3.25 fps to 3.50 fps, 3.50 fps to 3.75 fps, 3.75 fps to 4.00 fps, 4.00fps to 4.25 fps, 4.25 fps to 4.50 fps, 4.50 fps to 4.75 fps, 4.75 fps to5.00 fps, 5.00 fps to 5.25 fps, 5.25 fps to 5.50 fps, 5.50 fps to 5.75fps, 5.75 fps to 6.00 fps, 6.00 fps to 6.25 fps, 6.25 fps to 6.50 fps,6.50 fps to 6.75 fps, 6.75 fps to 7.00 fps, 7.00 fps to 7.25 fps, 7.25fps to 7.50 fps, 7.50 fps to 7.75 fps, 7.75 fps to 8.00 fps, 8.00 fps to8.25 fps, 8.25 fps to 8.50 fps, 8.50 fps to 8.75 fps, 8.75 fps to 9.00fps, 9.00 fps to 9.25 fps, 9.25 fps to 9.50 fps, 9.50 fps to 9.75 fps,or 9.75 fps to 10.00 fps.

In embodiments, the drain conduit (111*) is connected at one end to thefirst growing assembly (100*) via a drain port (110*) and connected atanother end to the common reservoir (500*) via a common drain conduit(517*). In embodiments, the drain conduit (211*) is connected at one endto the second growing assembly (200*) via a drain port (210*) andconnected at another end to the common reservoir (500*) via a commondrain conduit (517*). The common drain conduit (517*) is connected atone end to the common reservoir (500*) via a drain input (518*) and atanother end to the first drain conduit (111*) via a first drainconnection (112*). The common drain conduit (517*) is connected at oneend to the common reservoir (500*) via a drain input (518*) and atanother end to the second drain conduit (211*) via a second drainconnection (212*). In embodiments, the common drain conduit (517*) isconnected to both drain conduits (111*, 211*) from both growingassemblies (100*, 200*) and is configured to combine the liquid contentsof both drain conduits (111*, 211*) prior to introducing them into thecommon reservoir (500*). In embodiments, as shown in FIG. 8′, there isno common drain conduit (517*) and each drain conduit (111*, 211*) ofthe growing assemblies (100*, 200*) drains directly into the commonreservoir (500*).

The interior of the common reservoir (500*) is configured to hold water,macro-nutrients (601*), micro-nutrients (701*) from a micro-nutrientsupply tank (700*), and a pH adjustment solution (801*). In embodiments,the common reservoir (500*) is equipped with a reservoir pH sensor(PHO*) that is configured to input a signal (XPHO*) to a computer(COMP). In embodiments, the acidity of the water is measured by thereservoir pH sensor (PHO*) and adjusted to a desirable range from 5.15to 6.75. In embodiments, the common reservoir (500*) is equipped with areservoir temperature sensor (T0) that is configured to input a signal(XT0) to a computer (COMP). In embodiments, the common reservoir (500*)is equipped with a reservoir oxygen emitter (EZ*) that is configured toinput a signal (XEZ*) to a computer (COMP). In embodiments, the commonreservoir (500*) is equipped with a reservoir electrical conductivitysensor (E1) that is configured to input a signal (XE1*) to a computer(COMP).

In embodiments, the common reservoir (500*) is equipped with a reservoirrecirculation pump (P0*) followed by a reservoir recirculation filter(F3*) to remove solids from the common reservoir (500*). In embodiments,the common reservoir (500*) is equipped with a reservoir heat exchanger(HX2*) to maintain a temperature of the liquid contents within thecommon reservoir (500*). In embodiments, the common reservoir (500*) isequipped with a reservoir recirculation pump (P0*) followed by areservoir heat exchanger (HX2*) to maintain a temperature of the liquidcontents within the common reservoir (500*). The common reservoir (500*)has a reservoir recirculation outlet (510*) that is connected to areservoir recirculation pump suction conduit (512*). The reservoirrecirculation pump suction conduit (512*) is connected to a reservoirrecirculation pump (P0*). The reservoir recirculation pump (P0*) isconnected to a reservoir recirculation pump discharge conduit (514*)that transfers liquid back to the common reservoir (500*) via areservoir recirculation inlet (516*). In embodiments, a reservoirrecirculation filter (F3*) is installed on the reservoir recirculationpump discharge conduit (514*). In embodiments, a reservoir heatexchanger (HX2*) is installed on the reservoir recirculation pumpdischarge conduit (514*). In embodiments, a reservoir heat exchanger(HX2*) is installed on the reservoir recirculation pump dischargeconduit (514*) after the reservoir recirculation filter (F3*). Inembodiments, the reservoir heat exchanger (HX2*) may increase thetemperature of the liquid passing through it. In embodiments, thereservoir heat exchanger (HX2*) may decrease the temperature of theliquid passing through it.

The common reservoir (500*) is connected to a pump (P1*) via a pumpsuction conduit (303). The pump suction conduit (303*) is connected atone end to the common reservoir (500*) via a reservoir transfer outlet(302*) and connected at the other end to the pump (P1*). The pump (P1*)is equipped with a motor (MP1*) and a controller (CP1*) which isconfigured to input and output a signal (XP1*) to and from a computer(COMP). A pump discharge conduit (304*) is connected to the pump (P1*).The liquid supply header (300*) may be synonymous with the pumpdischarge conduit (304*) in that they both accept a portion ofpressurized liquid that was provided by the pump (P1*).

In embodiments, a pressure tank (PT*) is installed on the pump dischargeconduit (304*). In embodiments, the pressure tank (PT*) may bepressurized by the pump (P1*). The pressure tank (PT*) serves as apressure storage reservoir in which a liquid is held under pressure. Thepressure tank (PT*) enables the system to respond more quickly to atemporary demand, and to smooth out pulsations created by the pump(P1*). In embodiments, the pressure tank (PT*) serves as accumulator torelieve the pump (P1*) from constantly operating. In embodiments, thepressure tank (PT*) is a cylindrical tank rated for a maximum pressureof 200 PSI or 600 PSI. In embodiments, the pressure tank (PT*) is acylindrical tank that has a length to diameter ratio ranging from 1.25to 2.5.

A level control discharge conduit (310*) is connected to the pumpdischarge conduit (304*) via a connection (311*). The level controldischarge conduit (310*) is configured to pump the contents of thecommon reservoir (500*) away from the system for any number of reasons.Clean-out, replenishing the liquid within the common reservoir (500*) orto bleed off some of the liquid contents within may be some purposes forutilizing the level control discharge conduit (310*). A filter (F4*) isinstalled on the level control discharge conduit (310*). A level controlvalve (LCV*) is installed on the level control discharge conduit (310*)and is equipped with a controller (CCV*) that sends a signal (XCV*) toor from the computer (COMP). The filter (F4*) preferably is installedupstream of the level control valve (LCV*) to that solids do not clogthe level control valve (LCV*). Preferably the connection (311*) for thelevel control discharge conduit (310*) is connected as close as possibleto the pump (P1*) on the pump discharge conduit (304*) so that if thefilters (F1*, F2*) on the pump discharge conduit (304*) clog, there isstill a way to drain liquid from the system. A waste treatment unit(312*) may be placed on the level control discharge conduit (310*) todestroy any organic molecules, waste, bacteria, protozoa, helminths, orviruses that may be present in the liquid. In embodiments, the wastetreatment unit (312*) is an ozone unit (313*) configured to destroyorganic molecules, waste, bacteria, protozoa, helminths, or viruses viaoxidation.

At least one filter (F1*, F2*) may be installed on the pump dischargeconduit (304). FIG. 1A′ shows two filters (F1*, F2*) configured tooperate in a cyclic-batch mode where when one is on-line in a first modeof normal operation, the other is off-line and undergoing a back-flushcycle in a second mode of operation. This is depicted in FIG. 1A′wherein the first filter (F1*) is on-line and filtering the liquiddischarged from the pump (P1*) while the second filter (F2*) isoff-line. The first filter (F1*) is shown to have a first filter inletvalve (FV1*) and a first filter outlet valve (FV2*) both of which areopen in FIG. 1′. The second filter (F2*) is shown to have a secondfilter inlet valve (FV3*) and a second filter outlet valve (FV4*) bothof which are shown in the closed position as indicted by darkened-incolor of the valves (FV3*, FV4*). The second filter (F2*) is shown inthe back-flush mode of operation while the first filter (F1*) is shownin the normal mode of operation. While in the back-flush mode ofoperation, the second filter (F2*) is shown accepting a source of liquidfrom the common reservoir (500*) via a filter back-flush supply conduit(306*).

The common reservoir (500*) is equipped with a filter back-flush outlet(307*) that is connected to a filter back-flush supply conduit (306*).The filter back-flush supply conduit (306*) is connected at one end tothe common reservoir (500*) via a filter back-flush outlet (307*) and atanother end to the filter back-flush pump (308*). The filter back-flushpump (308*) is connected to the filter back-flush discharge conduit(309*). The filter back-flush discharge conduit (309*) has a filterback-flush supply valve (FV5*) installed thereon to provide pressurizedliquid from the common reservoir (500*) to the second filter (F2*)operating in the second mode of back-flush operation. The filterback-flush supply valve (FV5*) provides liquid to the second filter inbetween the second filter outlet valve (FV4*) and the second filter(F2*) to back-flush the second filter (F2*). A filter back-flushdischarge valve (FV6*) is provided in between the second filter and thesecond filter inlet valve (FV3*) to flush solids that have accumulatedduring the first mode of normal operation.

A filter inlet pressure sensor (P2*) is installed on the pump dischargeconduit (304*) before the filters (F1*, F2*). The filter inlet pressuresensor (P2*) is configured to output a signal (XP2*) to the computer(COMP). A filter discharge pressure sensor (P3*) is installed on thepump discharge conduit (304*) after the filters (F1*, F2*). The filterdischarge pressure sensor (P2*) is configured to output a signal (XP3*)to the computer (COMP). Then the pressure drop across the filters (F1*,F2*) reached a threshold predetermined value, the filters (F1*, F2*)switch modes of operation from first to second and from second to first.

A first oxygen emitter (EZ1*) is installed on the pump discharge conduit(304*). In embodiments, the first oxygen emitter (EZ1*) is installed onthe pump discharge conduit (304*) after the filters (F1*, F2*). Thefirst oxygen emitter (EZ1*) is configured to output a signal (XEZ1*) tothe computer (COMP). The first oxygen emitter (EZ1*) oxygenates thewater passing through the pump discharge conduit (304*).

A liquid flow sensor (F0*) is installed on the pump discharge conduit(304*) after the filters (F1*, F2*). The liquid flow sensor (F0*) isconfigured to output a signal (XF0*) to the computer (COMP). The liquidflow sensor (F0*) measures the flow rate of water passing through thepump discharge conduit (304*).

In embodiments, the flow rate of water passing through the pumpdischarge conduit (304*) ranges from 0.01 gallons per minute (gpm) to0.02 gpm, 0.02 gpm to 0.03 gpm, 0.03 gpm to 0.04 gpm, 0.04 gpm to 0.05gpm, 0.05 gpm to 0.06 gpm, 0.05 gpm to 0.06 gpm, 0.06 gpm to 0.07 gpm,0.07 gpm to 0.08 gpm, 0.08 gpm to 0.09 gpm, 0.09 gpm to 0.1 gpm, 0.1 gpmto 0.15 gpm, 0.15 gpm to 0.2 gpm, 0.2 gpm to 0.25 gpm, 0.25 gpm to 0.3gpm, 0.3 gpm to 0.35 gpm, 0.35 gpm to 0.4 gpm, 0.4 gpm to 0.45 gpm, 0.45gpm to 0.5 gpm, 0.5 gpm to 0.6 gpm, 0.6 gpm to 0.7 gpm, 0.7 gpm to 0.8gpm, 0.8 gpm to 0.9 gpm, 0.9 gpm to 1 gpm, 1 gpm to 2 gpm, 2 gpm to 3gpm, 3 gpm to 4 gpm, 4 gpm to 5 gpm, 5 gpm to 6 gpm, 6 gpm to 7 gpm, 7gpm to 8 gpm, 8 gpm to 9 gpm, 9 gpm to 10 gpm, 10 gpm to 11 gpm, 11 gpmto 12 gpm, 12 gpm to 13 gpm, 13 gpm to 14 gpm, 14 gpm to 15 gpm, 15 gpmto 16 gpm, 16 gpm to 17 gpm, 17 gpm to 18 gpm, 18 gpm to 19 gpm, 19 gpmto 20 gpm, 20 gpm to 30 gpm, 30 gpm to 40 gpm, 40 gpm to 50 gpm, 50 gpmto 60 gpm, 60 gpm to 70 gpm, 70 gpm to 80 gpm, 80 gpm to 90 gpm, 90 gpmto 100 gpm, 100 gpm to 125 gpm, 125 gpm to 150 gpm, 150 gpm to 175 gpm,175 gpm to 200 gpm, 200 gpm to 225 gpm, 225 gpm to 250 gpm, 250 gpm to275 gpm, 275 gpm to 300 gpm, 300 gpm to 350 gpm, 350 gpm to 400 gpm, 400gpm to 450 gpm, 450 gpm to 500 gpm, 500 gpm to 550 gpm, 550 gpm to 600gpm, 600 gpm to 650 gpm, 650 gpm to 700 gpm, 700 gpm to 750 gpm, 750 gpmto 800 gpm, 800 gpm to 850 gpm, 850 gpm to 900 gpm, 900 gpm to 950 gpm,950 gpm to 1000 gpm, 1000 gpm to 1500 gpm, 1500 gpm to 2000 gpm, 2000gpm to 2500 gpm, 2500 gpm to 3000 gpm, 3000 gpm to 3500 gpm, 3500 gpm to4000 gpm, 4000 gpm to 4500 gpm, 4500 gpm to 5000 gpm, 5000 gpm to 5500gpm, 5500 gpm to 6000 gpm, 6000 gpm to 6500 gpm, 6500 gpm to 7000 gpm,7000 gpm to 7500 gpm, 7500 gpm to 8000 gpm, 8000 gpm to 8500 gpm, 8500gpm to 9000 gpm, 9000 gpm to 9500 gpm, or 9500 gpm to 10000 gpm.

In embodiments, the velocity of the water passing through the pumpdischarge conduit (304*) ranges from 3.00 fps to 3.25 fps, 3.25 fps to3.50 fps, 3.50 fps to 3.75 fps, 3.75 fps to 4.00 fps, 4.00 fps to 4.25fps, 4.25 fps to 4.50 fps, 4.50 fps to 4.75 fps, 4.75 fps to 5.00 fps,5.00 fps to 5.25 fps, 5.25 fps to 5.50 fps, 5.50 fps to 5.75 fps, 5.75fps to 6.00 fps, 6.00 fps to 6.25 fps, 6.25 fps to 6.50 fps, 6.50 fps to6.75 fps, 6.75 fps to 7.00 fps, 7.00 fps to 7.25 fps, 7.25 fps to 7.50fps, 7.50 fps to 7.75 fps, 7.75 fps to 8.00 fps, 8.00 fps to 8.25 fps,8.25 fps to 8.50 fps, 8.50 fps to 8.75 fps, 8.75 fps to 9.00 fps, 9.00fps to 9.25 fps, 9.25 fps to 9.50 fps, 9.50 fps to 9.75 fps, or 9.75 fpsto 10.00 fps.

In embodiments, the velocity of the water passing through the pumpsuction conduit (303) ranges from 0.25 feet per second (fps) to 0.50fps, 0.50 fps to 0.75 fps, 0.75 fps to 1.00 fps, 1.00 fps to 1.25 fps,1.25 fps to 1.50 fps, 1.50 fps to 1.75 fps, 1.75 fps to 2.00 fps, 2.00fps to 2.25 fps, 2.25 fps to 2.50 fps, 2.50 fps to 2.75 fps, or 2.75 fpsto 3.00 fps.

A growing assembly liquid supply valve (V1*) is installed on the pumpdischarge conduit (304*). In embodiments, the growing assembly liquidsupply valve (V1*) is installed on the pump discharge conduit (304*)after the filters (F1*, F2*). The growing assembly liquid supply valve(V1*) is equipped with a controller (CV1*) that sends a signal (XV1*) toor from a computer (COMP).

An electrical conductivity sensor (E2*) is installed on the pumpdischarge conduit (304*). In embodiments, the electrical conductivitysensor (E2*) is installed on the pump discharge conduit (304*) after thefilters (F1*, F2*). The electrical conductivity sensor (E2*) isconfigured to output a signal (XE2*) to the computer (COMP). Theelectrical conductivity sensor (E2*) measures the electricalconductivity of the water passing through the pump discharge conduit(304*).

A liquid heat exchanger (HX3*) is installed on the pump dischargeconduit (304*). In embodiments, the liquid heat exchanger (HX3*) isinstalled on the pump discharge conduit (304*) after the filters (F1*,F2*). The liquid heat exchanger (HX3*) is configured increase ordecrease the temperature of the water passing through the pump dischargeconduit (304*).

A liquid temperature sensor (T3*) is installed on the pump dischargeconduit (304*). In embodiments, the liquid temperature sensor (T3*) isinstalled on the pump discharge conduit (304*) after the filters (F1*,F2*). In embodiments, the liquid temperature sensor (T3*) is installedon the pump discharge conduit (304*) after the liquid heat exchanger(HX3*). The liquid temperature sensor (T3*) is configured to input asignal (XT3*) to the computer (COMP).

In embodiments, the growing assembly liquid supply valve (V1*), firstgrowing assembly liquid supply valve (V3*), and/or the second growingassembly liquid supply valve (V4*), may continuously be open to permit acontinuous flow of liquid into the growing assemblies (100*, 200*). Inembodiments, the growing assembly liquid supply valve (V1*), firstgrowing assembly liquid supply valve (V3*), and/or second growingassembly liquid supply valve (V4*), may be opened and closed by theircontrollers (CV1*, CV3*, CV4*) and operated by a computer (COMP). Inembodiments, the growing assembly liquid supply valve (V1*), firstgrowing assembly liquid supply valve (V3*), and/or second growingassembly liquid supply valve (V4*), may be opened and closed by theircontrollers (CV1*, CV3*, CV4*) and operated by a computer (COMP) on atimer.

It is preferred to have the valves (V1*, V3*, V4*) operated in aplurality of modes of operation. In embodiments, a first mode ofoperation includes having the growing assembly liquid supply valve(V1*), first growing assembly liquid supply valve (V3*), second growingassembly liquid supply valve (V4*), all in an open valve position totransfer liquid from the common reservoir (500*) into the growingassemblies (100*, 200*). In embodiments, a second mode of operationincludes having the growing assembly liquid supply valve (V1*) open,first growing assembly liquid supply valve (V3*) closed, and secondgrowing assembly liquid supply valve (V4*) closed, to stop the transferliquid to the growing assemblies (100*, 200*). In embodiments, a thirdmode of operation includes having the growing assembly liquid supplyvalve (V1*) open, first growing assembly liquid supply valve (V3*) open,second growing assembly liquid supply valve (V4*) closed, to transferliquid to the first growing assembly (100*) and not into the secondgrowing assembly (200*). In embodiments, a fourth mode of operationincludes having the growing assembly liquid supply valve (V1*) open,first growing assembly liquid supply valve (V3*) closed, second growingassembly liquid supply valve (V4*) open, to transfer liquid to thesecond growing assembly (200*) and not into the first growing assembly(100*).

In embodiments, the farming superstructure system (FSS) is operated in amanner that switches from one mode of operation to another mode ofoperation. In embodiments, the farming superstructure system (FSS) isoperated in a manner that switches on a cyclical basis from: a firstmode of operation to the second mode of operation; a second mode ofoperation to the first mode of operation. In embodiments, the farmingsuperstructure system (FSS) is operated in a manner that switches on acyclical basis from: a third mode of operation to the fourth mode ofoperation; a fourth mode of operation to the third mode of operation. Itis preferred to turn on and off at least one of the valves (V1*, V3*,V4*) in a cyclical manner to permit to prevent the roots of the cannabisfrom receiving too much mist or spray.

In embodiments, the first mode of operation lasts for 5 seconds openfollowed by the second mode of operation lasting for 600 seconds closed.In embodiments, the third mode of operation lasts for 5 seconds openfollowed by the fourth mode of operation lasting for 600 seconds closed.In embodiments, water is transferred to the first growing assembly(100*) for 5 seconds followed by not transferring water to the firstgrowing assembly (100*) for 600 seconds. In embodiments, water istransferred to the second growing assembly (200*) for 5 seconds followedby not transferring water to the second growing assembly (200*) for 600seconds. In embodiments, water is transferred to both the first andsecond growing assemblies (100*, 200*) for 5 seconds followed by nottransferring water to both the first and second growing assemblies(100*, 200*) for 600 seconds. 5 divided by 600 is 0.008.

In embodiments, the first mode of operation lasts for 60 seconds openfollowed by the second mode of operation lasting for 180 seconds closed.In embodiments, the third mode of operation lasts for 60 seconds openfollowed by the fourth mode of operation lasting for 180 seconds closed.In embodiments, water is transferred to the first growing assembly(100*) for 60 seconds followed by not transferring water to the firstgrowing assembly (100*) for 180 seconds. In embodiments, water istransferred to the second growing assembly (200*) for 60 secondsfollowed by not transferring water to the second growing assembly (200*)for 180 seconds. 60 divided by 180 is 0.333.

The duration of time when liquid is transferred to at least one growingassembly (100*, 200*) divided by the duration of time when liquid is nottransferred to at least one growing assembly (100*, 200*) may beconsidered an open-close ratio. The open-close ratio may be the durationof time when at least one valve (V1*, V3*, V4*) is open in secondsdivided by the subsequent duration of time when the same valve is closedin seconds before the same valve opens again. In embodiments, theopen-close ratio ranges from between 0.008 to 0.33. In embodiments, thecomputer (COMP) opens and closes the valve (V1*, V3*, V4*) toperiodically introduce the pressurized liquid mixture into to eachgrowing assembly with an open-close ratio ranging from between 0.008 to0.33, the open-close ratio is defined as the duration of time when thevalve (V1*, V3*, V4*) is open in seconds divided by the subsequentduration of time when the same valve is closed in seconds before thesame valve opens again. The computer (COMP) opens and closes the valves(V1*, V3*, V4*) to periodically introduce the pressurized liquid mixtureinto to each growing assembly with an open-close ratio ranging frombetween 0.008 to 0.33.

In embodiments, the open-close ratio varies. The open-close ratio mayvary throughout the life of the cannabis contained within the growingassemblies (100*, 200*). The open-close ratio may vary throughout thestage of development of the cannabis contained within the growingassemblies (100*, 200*). Stages of development of the cannabis includeflowering, pollination, fertilization. In embodiments, the open-closeratio is greater during flowering and less during pollination. Inembodiments, the open-close ratio is greater during pollination and lessduring fertilization. In embodiments, the open-close ratio is greaterduring flowering and less during fertilization. In embodiments, theopen-close ratio is less during flowering and greater duringpollination. In embodiments, the open-close ratio is less duringpollination and greater during fertilization. In embodiments, theopen-close ratio is less during flowering and greater duringfertilization.

In embodiments, the temperature is greater during flowering and lessduring pollination. In embodiments, the temperature is greater duringpollination and less during fertilization. In embodiments, thetemperature is greater during flowering and less during fertilization.In embodiments, the temperature is less during flowering and greaterduring pollination. In embodiments, the temperature is less duringpollination and greater during fertilization. In embodiments, thetemperature is less during flowering and greater during fertilization.

The open-close ratio may vary throughout a 24-hour duration of time. Inembodiments, the open-close ratio is increased during the day-time anddecreased during the night-time relative to one another. In embodiments,the open-close ratio varies increased during the night-time anddecreased during the day-time relative to one another. Night-time isdefined as the time between evening and morning. Day-time is defined asthe time between morning and evening.

In embodiments, carbohydrates may be added to the common reservoir(500). The carbohydrates are comprised of one or more from the groupconsisting of sugar, sucrose, molasses, and plant syrups. Inembodiments, enzymes may be added to the common reservoir (500). Theenzymes are comprised of one or more from the group consisting of aminoacids, orotidine 5′-phosphate decarboxylase, OMP decarboxylase,glucanase, beta-glucanase, cellulase, xylanase, HYGROZYME®, CANNAZYME®,MICROZYME®, and SENSIZYME®. In embodiments, vitamins may be added to thecommon reservoir (500*). The vitamins are comprised of one or more fromthe group consisting of vitamin B, vitamin C, vitamin D, and vitamin E.In embodiments, hormones may be added to the common reservoir (500*).The hormones are comprised of one or more from the group consisting ofauxins, cytokinins gibberellins, abscic acid, brassinosteroids,salicylic acid, jasmonates, plant peptide hormones, polyamines, nitricoxide, strigolactones, and triacontanol. In embodiments, microorganismsmay be added to the common reservoir (500*). The microorganisms arecomprised of one or more from the group consisting of bacteria,diazotroph bacteria, diazotrop archaea, azotobacter vinelandii,clostridium pasteurianu, fungi, arbuscular mycorrhizal fungi, glomusaggrefatum, glomus etunicatum, glomus intraradices, rhizophagusirregularis, and glomus mosseae.

In embodiments, an analyzer (AZ*) may be incorporated into the farmingsuperstructure system (FSS). In embodiments, the analyzer analyzes thecontents within the common reservoir (500*) of analyzes the mixture ofwater, macro-nutrients, micro-nutrients, and a pH adjustment solution todetermine the whether any water, macro-nutrients, micro-nutrients, and apH adjustment need to be added. A signal (XAZ*) from the analyzer may besent to a computer (COMP). From the signal (XAZ*) obtained by thecomputer (COMP), the computer (COMP) may calculate and automate theintroduction of water, macro-nutrients, micro-nutrients, and a pHadjustment solution introduced to the system. In embodiments, theanalyzer (AZ*) may include a mass spectrometer, Fourier transforminfrared spectroscopy, infrared spectroscopy, potentiometric pH meter,pH meter, electrical conductivity meter, or liquid chromatography.

FIG. 1B′

FIG. 1B′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) that includes a first growing assembly (100*) having afirst growing medium (GM1*) and a second growing assembly (200*) havinga second growing medium (GM2*).

In embodiments, the first and second growing mediums (GM1*, GM2*) can becomprised of one or more from the group consisting of rockwool, perlite,amorphous volcanic glass, vermiculite, clay, clay pellets, LECA(lightweight expanded clay aggregate), coco-coir, fibrous coconut husks,soil, dirt, peat, peat moss, sand, soil, compost, manure, fir bark,foam, gel, oasis cubes, lime, gypsum, and quartz.

In embodiments, the first and second growing mediums (GM1*, GM2*) can becomprised of one or more from the group consisting of: a PH adjuster,amorphous volcanic glass, aged forest materials, aged forest products,aged redwood tree bark, aged redwood tree chips, aged coniferous treebark, aged coniferous tree chips, alfalfa meal, basalt, bat guano, cocochips, coco fiber, compost, composted chicken manure, composted manure,dolomite, feather meal, fish bone meal, fish scales, gypsum, kelp meal,lava rock, mafic extrusive igneous rock, perlite, protein, rockwool,sphagnum peat moss. In embodiments, psilocybin mushrooms are growingwithin the growing medium within the Farming Superstructure System(FSS).

In embodiments, a fungus may be added to the growing medium. Inembodiment, the fungus may be mycorrhiza. In embodiments, the first andsecond growing mediums (GM1*, GM2*) can be comprised of a liquid andincludes water. In embodiments, the first and second growing mediums(GM1*, GM2*) can be comprised of a liquid and includes water andincludes a hydroponic system.

FIG. 1B′ differs from FIG. 1A′ since a fabric (104*, 204*) does notpartition the growing assembly (100*, 200*) into an upper-section (105*,205*) and a lower-section (106*, 206*). Instead, the cannabis (107*,207*) are in contact with the growing medium (GM1*, GM2*), and thegrowing medium (GM1*, GM2*) partitions each growing assembly (100*,200*) into an upper-section (105*, 205*) and a lower-section (106*,206*). Liquid from with pump (P1*) is introduced into the interior(101*, 201*) of each growing assembly (100*, 200*) via a liquid input(114*, 214*) where the liquid contacts the growing medium (GM1*, GM2*).In embodiments, liquid from the pump (P1*) is the growing medium (GM1*,GM2*). In embodiments, liquid is transferred to the interior (101*,201*) of each growing assembly (100*, 200*) via the liquid input (114*,214*) on a periodic basis.

In embodiments, the computer (COMP) controls the lights (L1*, L2*). Inembodiments, the lights (L1*, L2*) illuminate each growing assembly(100,* 200*) with an illumination on-off ratio ranging from between 0.5to 11. The illumination on-off ratio is defined as the duration of timewhen the lights (L1*, L2*) are on and illuminate the cannabis (107*,207*) in hours divided by the subsequent duration of time when thelights (L1*, L2*) are off and are not illuminating the cannabis (107*,207*) in hours before the lights are turned on again.

In embodiments, the lights (L1*, L2*) are on and illuminate the cannabisfor 18 hours and then are turned off for 6 hours. 18 divided by 6 is 3.In embodiments, an illumination on-off ratio of 3 is contemplated. Inembodiments, the lights (L1*, L2*) are on and illuminate the cannabisfor 20 hours and then are turned off for 4 hours. 20 divided by 4 is 5.In embodiments, an illumination on-off ratio of 5 is contemplated. Inembodiments, the lights (L1*, L2*) are on and illuminate the cannabisfor 24 hours and then are turned off for 0 hours. In embodiments, thelights (L1*, L2*) are on and illuminate the cannabis for 24 hours andthen are turned off for 0 hours, wherein the lights include blue lights.24 divided by 0 is 0. In embodiments, an illumination on-off ratio of 0is contemplated. In embodiments, the lights (L1*, L2*) are on andilluminate the cannabis for 22 hours and then are turned off for 2hours. 22 divided by 2 is 11. In embodiments, an illumination on-offratio of 11 is contemplated. In embodiments, the lights (L1*, L2*) areon and illuminate the cannabis for 8 hours and then are turned off for16 hours. 8 divided by 16 is 0.5. In embodiments, an illumination on-offratio of 0.5 is contemplated. In embodiments, the lights (L1*, L2*) areon and illuminate the cannabis for 12 hours and then are turned off for12 hours. 12 divided by 12 is 1. In embodiments, an illumination on-offratio of 1 is contemplated. In embodiments, the is desirable to operatethe growing assemblies at an illumination on-off ratio that is greaterthan 1 and less than 11. In embodiments, the is desirable to operate thegrowing assemblies at an illumination on-off ratio that is greater than0.5 and equal to or less than 5. In embodiments, the is desirable tooperate the growing assemblies at an illumination on-off ratio rangesfrom 0 to 5.

In embodiments, each growing assembly (100*, 200*) may include acontainer that contains a growing medium (GM1*, GM2*) sufficient tosupport the roots of the cannabis (107*, 207*). In embodiments, thegrowing assembly (100*, 200*) may be a container that contains a growingmedium (GM1*, GM2*).

FIG. 1C′

FIG. 1C′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) that includes a first growing assembly (100*) having afirst growing medium (GM1*) and a second growing assembly (200*) havinga second growing medium (GM2*) and the first growing assembly (100*) andsecond growing assembly (200*) are grown outdoors.

FIG. 1C′ shows a fabric (104*, 204*) that is placed upon the firstgrowing medium (GM1*) and the second growing medium (GM2*). Inembodiments, the fabric (104*, 204*) is landscape fabric that includes atextile material used to control weeds by inhibiting their exposure tosunlight. In embodiments, the fabric (104*, 204*) is placed around thatcannabis plants (107*, 207*), covering areas where other growth isunwanted. The fabric itself can be made from plastic, rubber, syntheticor organic materials, sometimes from recycled sources. In embodiments,the fabric (104*, 204*) is woven needle punch polypropylene fabric. Inembodiments, the fabric (104*, 204*) is black.

In embodiments, liquid is transferred to the first growing assembly(100*) and second growing assembly (200*) on a periodic basic throughthe plurality of liquid supply conduits (113*, 213*), the liquid supplyheader (300*), at least one filter (F1*, F2*), and at least one valvevalves (V1*, V3*, V4*). In embodiments, the spacing (CAA*, CAB, CAC*,CAD*) between each plant (107A*, 107B*, 107C*, 207A*, 207B*, 207C*)includes one or more plant spacing ranges selected from the groupconsisting of 1.00 foot to 1.25 feet, 1.25 feet to 1.50 feet, 1.50 feetto 1.75 feet, 1.75 feet to 2.00 feet, 2.00 feet to 2.25 feet, 2.25 feetto 2.50 feet, 2.50 feet to 2.75 feet, 2.75 feet to 3.00 feet, 3.00 feetto 3.25 feet, 3.25 feet to 3.50 feet, 3.50 feet to 3.75 feet, 3.75 feetto 4.00 feet, 4.00 feet to 4.25 feet, 4.25 feet to 4.50 feet, 4.50 feetto 4.75 feet, 4.75 feet to 5.00 feet, 5.00 feet to 5.25 feet, 5.25 feetto 5.50 feet, 5.50 feet to 5.75 feet, 5.75 feet to 6.00 feet, 6.00 feetto 6.25 feet, 6.25 feet to 6.50 feet, 6.50 feet to 6.75 feet, 6.75 feetto 7.00 feet, 7.00 feet to 7.25 feet, 7.25 feet to 7.50 feet, 7.50 feetto 7.75 feet, and 7.75 feet to 8.00 feet, 8 feet to 10 feet, 10 feet to12 feet, 12 feet to 15 feet, 15 feet to 30 feet.

In embodiments, the cannabis plants may be grown with additional plantsto improve soil health and decrease evaporation of water from thegrowing medium. The cannabis plants may be indoors within the interiorof the enclosure or outdoors for additional plants to improve soilhealth and decrease evaporation of water from the growing medium. Inembodiments, the additional plants include clover, wild flowers,flowers, shamrock, legumes, nitrogen fixing plants, beans, peas. Inembodiments, the additional plants also promote insect health. Inembodiments, the additional plants also promote pollination of cannabisplants and or the additional plants.

FIG. 1D′

FIG. 1D′ depicts one non-limiting embodiment general arrangement of afarming superstructure system (FSS) top-view that includes a firstgrowing assembly (100*) and a second growing assembly (200*) eachconfigured to grow plants (107*, 107A*, 107B*, 107C*, 207*, 207A*,207B*, 207C*).

FIG. 1D′ shows a top-down-view of one-acre plot of the farmingsuperstructure system (FSS). In embodiments, the acre (DAA)* has alength (DAB*) and a width (DAC*). The acre is a unit of land area usedin the imperial and US customary systems. In embodiments, the acre is asquare enclosing one acre is approximately 69.57 yards, or 208 feet 9inches (63.61 meters) on a side. As a unit of measure, an acre has noprescribed shape; any area of 43,560 square feet is an acre. Inembodiments, the acre (DAA*) has a length (DAB*) of 208 feet 9 inches.In embodiments, the acre (DAA*) has a width (DAC*) of 208 feet 9 inches.

In embodiments, the width of the fabric (104*, 204*) includes one ormore fabric widths (DAD*, DAE*) selected from the group consisting of1.00 foot to 1.25 feet, 1.25 feet to 1.50 feet, 1.50 feet to 1.75 feet,1.75 feet to 2.00 feet, 2.00 feet to 2.25 feet, 2.25 feet to 2.50 feet,2.50 feet to 2.75 feet, 2.75 feet to 3.00 feet, 3.00 feet to 3.25 feet,3.25 feet to 3.50 feet, 3.50 feet to 3.75 feet, 3.75 feet to 4.00 feet,4.00 feet to 4.25 feet, 4.25 feet to 4.50 feet, 4.50 feet to 4.75 feet,4.75 feet to 5.00 feet, 5 feet to 6 feet, 6 feet to 8 feet, 8 feet to 10feet, 10 feet to 12 feet, 12 feet to 14 feet, 14 feet to 16 feet, 16feet to 20 feet.

In embodiments, the spacing (CAA*, CAB*, CAC*, CAD*) between each plant(107A*, 107B*, 107C*, 207A*, 207B*, 207C*) includes one or more plantspacing ranges selected from the group consisting of 1.00 foot to 1.25feet, 1.25 feet to 1.50 feet, 1.50 feet to 1.75 feet, 1.75 feet to 2.00feet, 2.00 feet to 2.25 feet, 2.25 feet to 2.50 feet, 2.50 feet to 2.75feet, 2.75 feet to 3.00 feet, 3.00 feet to 3.25 feet, 3.25 feet to 3.50feet, 3.50 feet to 3.75 feet, 3.75 feet to 4.00 feet, 4.00 feet to 4.25feet, 4.25 feet to 4.50 feet, 4.50 feet to 4.75 feet, 4.75 feet to 5.00feet, 5.00 feet to 5.25 feet, 5.25 feet to 5.50 feet, 5.50 feet to 5.75feet, 5.75 feet to 6.00 feet, 6.00 feet to 6.25 feet, 6.25 feet to 6.50feet, 6.50 feet to 6.75 feet, 6.75 feet to 7.00 feet, 7.00 feet to 7.25feet, 7.25 feet to 7.50 feet, 7.50 feet to 7.75 feet, 7.75 feet to 8.00feet, 8 feet to 9 feet, 9 feet to 10 feet, 10 feet to 11 feet, 11 feetto 12 feet, 12 feet to 13 feet, 13 feet to 14 feet, and 14 feet to 15feet.

In embodiments, the spacing (CAA*, CAB*, CAC*, CAD*) between eachgrowing assembly (100*, 200*) includes one or more growing assemblyspacing ranges (DAF*) selected from the group consisting of 2.00 feet to3.00 feet, 3.00 feet to 3.25 feet, 3.25 feet to 3.50 feet, 3.50 feet to3.75 feet, 3.75 feet to 4.00 feet, 4.00 feet to 4.25 feet, 4.25 feet to4.50 feet, 4.50 feet to 4.75 feet, 4.75 feet to 5.00 feet, 5.00 feet to5.25 feet, 5.25 feet to 5.50 feet, 5.50 feet to 5.75 feet, 5.75 feet to6.00 feet, 6.00 feet to 6.25 feet, 6.25 feet to 6.50 feet, 6.50 feet to6.75 feet, 6.75 feet to 7.00 feet, 7.00 feet to 7.25 feet, 7.25 feet to7.50 feet, 7.50 feet to 7.75 feet, 7.75 feet to 8.00 feet, 8.00 feet to8.25 feet, 8.25 feet to 8.50 feet, 8.50 feet to 8.75 feet, 8.75 feet to9.00 feet, 9.00 feet to 9.25 feet, 9.25 feet to 9.50 feet, 9.50 feet to9.75 feet, 9.75 feet to 10.00 feet, 10 feet to 11 feet, 11 feet to 12feet, 12 feet to 13 feet, 13 feet to 14 feet, and 14 feet to 15 feet.

In embodiments, the amount of growing assemblies (102*, 207*) per acreinclude one or more ranges of rows of plants per acre selected from thegroup consisting of 70 rows of plants per acre to 64 rows of plants peracre, 64 rows of plants per acre to 60 rows of plants per acre, 60 rowsof plants per acre to 56 rows of plants per acre, 56 rows of plants peracre to 52 rows of plants per acre, 52 rows of plants per acre to 49rows of plants per acre, 49 rows of plants per acre to 46 rows of plantsper acre, 46 rows of plants per acre to 44 rows of plants per acre, 44rows of plants per acre to 42 rows of plants per acre, 42 rows of plantsper acre to 40 rows of plants per acre, 40 rows of plants per acre to 38rows of plants per acre, 38 rows of plants per acre to 36 rows of plantsper acre, 36 rows of plants per acre to 35 rows of plants per acre, 35rows of plants per acre to 33 rows of plants per acre, 33 rows of plantsper acre to 32 rows of plants per acre, 32 rows of plants per acre to 31rows of plants per acre, 31 rows of plants per acre to 30 rows of plantsper acre, 30 rows of plants per acre to 29 rows of plants per acre, 29rows of plants per acre to 28 rows of plants per acre, 28 rows of plantsper acre to 27 rows of plants per acre, 27 rows of plants per acre to 26rows of plants per acre, 26 rows of plants per acre to 25 rows of plantsper acre, 25 rows of plants per acre to 25 rows of plants per acre, 25rows of plants per acre to 24 rows of plants per acre, 24 rows of plantsper acre to 23 rows of plants per acre, 23 rows of plants per acre to 23rows of plants per acre, 23 rows of plants per acre to 22 rows of plantsper acre, 22 rows of plants per acre to 21 rows of plants per acre, 21rows of plants per acre to 20 rows of plants per acre, and at most 20rows of plants per acre. FIG. 1D′ shows only 7 rows of plants per acrefor simplicity but many more may be used as described and disclosedherein.

FIG. 2′

FIG. 2′ depicts one non-limiting embodiment of a farming superstructuresystem (FSS) including a first vertically stacked system (1500*)including a plurality of vertically stacked growing assemblies (100*,200*) integrated with a first and second vertical support structure(VSS1*, VSS2*) wherein the first growing assembly (100*) is supported bya first horizontal support structure (SS1*) and a second growingassembly (200*) is supported by a second horizontal support structure(SS2*).

The first vertically stacked system (1500*) shown in FIG. 2′ has a baseheight (H0*) located on a floor or support surface. The first verticallystacked system (1500*) shown in FIG. 2′ has a total height (HT*). Inembodiments, the total height (HT*) may be dictated by the total heightof the first and second vertical support structure (VSS1*, VSS2*). Thecommon reservoir (500*) may be positioned on the base height (H0*)located on a floor or support surface. The common reservoir (500*) has aliquid level (LIQ*) that is located below the reservoir height (H500*).The reservoir height (H500*) is the height of the common reservoir(500*).

The bottom (103*) of the first growing assembly (100*) is located at afirst base height (H100A*). The first base height (H100A*) is thevertical location on the first vertically stacked system (1500*) wherethe first growing assembly (100*) is supported by a first horizontalsupport structure (SS1*). The first partition height (H100B*) is thevertical location on the first vertically stacked system (1500*) of thepartition (104*) of the first growing assembly (100*). The first growingassembly height (H100C*) is the vertical location on the firstvertically stacked system (1500*) where the top (102*) of the firstgrowing assembly (100*) is located.

The second base height (H200A*) is the vertical location on the firstvertically stacked system (1500*) where the second growing assembly(200*) is supported by a second horizontal support structure (SS2*). Thesecond partition height (H200B*) is the vertical location on the firstvertically stacked system (1500*) of the partition (204*) of the secondgrowing assembly (200*). The second growing assembly height (H100C*) isthe vertical location on the first vertically stacked system (1500*)where the top (202*) of the second growing assembly (200*) is located.

The first vertically stacked system (1500*) has a width (W1500*). Inembodiments, the width (W1500*) is greater than the difference betweenthe first growing assembly height (H100C*) and the first base height(H100A*). In embodiments, the width (W1500*) is greater than thedifference between the second growing assembly height (H200C*) and thesecond base height (H200A*).

FIG. 3′

FIG. 3′ depicts one non-limiting embodiment of a plurality of verticallystacked systems (1500*, 1500′*) including a first vertically stackedsystem (1500*) and a second vertically stacked system (1500′*), thefirst vertically stacked system (1500*) as depicted in FIG. 2′, alsoboth vertically stacked systems (1500*, 1500′*) are contained within anenclosure (ENC*) having an interior (ENC1).

In embodiments, the interior (ENC1*) of the enclosure (ENC*) of thefarming superstructure system (FSS) (disclosed in Volume II) is also theinterior (ENC1) of the enclosure (ENC) of the feeding chamber (200) ofthe Insect Production Superstructure System (IPSS) (disclosed in VolumeI). In embodiments, insects (INS*) live within the interior (ENC1*) ofthe enclosure (ENC*) of the farming superstructure system (FSS) and theinsects (INS*) include one or more selected from the group consisting ofAnthocoridae, minute pirate bugs, pirate bugs, flower bugs, the genusOrius, omnivorous bugs, carnivorous bugs, Orthoptera order of insects,grasshoppers, crickets, katydids, weta, lubber, acrida, locusts, mites,spider mites, predatory mites, Neoseiulus Fallacis, genus of mites thatare in the Phytoseiidae family, arthropods, hexapods, beetles, cicadas,beetles, nematodes, mealworms, bats, mammals of the order Chiroptera,yellow mealworm beetles, Tenebrio Molitor, Tetranychus Urticae,carnivorous arthropods, omnivorous arthropods, green lacewings, insectsin the family Chrysopidae, insects in the order Neuroptera, mantidflies,antlions, Encarsia Formosa, whitefly parasites, ladybugs, spiders,orb-weaving spiders, arachnids, members of the spider family Araneidae,praying mantis, arachnids, eight-legged arthropods, and six-leggedarthropods. In embodiments, insects (INS*) live within the interior(ENC1*) of the enclosure (ENC*) of the farming superstructure system(FSS) protect the plants (107*, 207*) by feeding on other insect eggs,insect larva, and other insects including living organisms which may ormay not contain chitin not only including spider mites, rust mites,thrips, jumping plant lice, white fly, knats, gnats, aphids, andinsects. In embodiments, the insects feed on thrips order Thysanoptera.In embodiments, the insects (INS*) within the farming superstructuresystem (FSS) feed on Tetranychus Urticae. In embodiments, the insects(INS*) within the farming superstructure system (FSS) feed on spidermites. In embodiments, the insects (INS*) within the farmingsuperstructure system (FSS) eat other insects that are found on thecannabis plants disclosed herein. In embodiments, the bats eat insectsthat are found on the cannabis plants disclosed herein.

The second vertically stacked system (1500′*) shown in FIG. 3′ has abase height (H0*) located on a floor or support surface. The secondvertically stacked system (1500′*) shown in FIG. 3′ has a total height(HT′*). In embodiments, the total height (HT′*) may be dictated by thetotal height of the first and second vertical support structure (VSS1′*,VSS2′*). The common reservoir (500′*) may be positioned on the baseheight (H0*) located on a floor or support surface. The common reservoir(500′*) has a liquid level (LIQ′*) that is located below the reservoirheight (H500′*). The reservoir height (H500′*) is the height of thecommon reservoir (500*).

The bottom (103′*) of the first growing assembly (100′*) is located at afirst base height (H100A′*). The first base height (H100A′*) is thevertical location on the second vertically stacked system (1500′*) wherethe first growing assembly (100′*) is supported by a first horizontalsupport structure (SS1′*). The first partition height (H100B′*) is thevertical location on the second vertically stacked system (1500′*) ofthe partition (104′*) of the first growing assembly (100′*). The firstgrowing assembly height (H100C′*) is the vertical location on the secondvertically stacked system (1500′*) where the top (102′*) of the firstgrowing assembly (100′*) is located.

The second base height (H200A′*) is the vertical location on the secondvertically stacked system (1500′*) where the second growing assembly(200′*) is supported by a second horizontal support structure (SS2′*).The second partition height (H200B′*) is the vertical location on thesecond vertically stacked system (1500′*) of the partition (204′*) ofthe second growing assembly (200′*). The second growing assembly height(H100C′*) is the vertical location on the second vertically stackedsystem (1500′*) where the top (202′*) of the second growing assembly(200′*) is located.

The second vertically stacked system (1500′*) has a width (W1500′*). Inembodiments, the width (W1500′*) is greater than the difference betweenthe first growing assembly height (H100C′*) and the first base height(H100A′*). In embodiments, the width (W1500′*) is greater than thedifference between the second growing assembly height (H200′*) and thesecond base height (H200A′*).

A spacing (1500S*) exists between the first vertically stacked system(1500*) and the second vertically stacked system (1500′*). Inembodiments, the spacing (1500S*) between the first vertically stackedsystem (1500*) and second vertically stacked system (1500′*) is lessthan the width (W1500*, W1500′*) of either of the first verticallystacked system (1500*) and second vertically stacked system (1500′*). Inembodiments, the spacing (1500S*) between the first vertically stackedsystem (1500*) and second vertically stacked system (1500′*) is greaterthan the width (W1500*, W1500′*) of either of the first verticallystacked system (1500*) and second vertically stacked system (1500′*). Inembodiments, the spacing (1500S*) between the first vertically stackedsystem (1500*) and second vertically stacked system (1500′*) rangesbetween 1 foot to 2 feet, 2 feet to 3 feet, 3 feet to 4 feet, 4 feet to5 feet, 5 feet to 6 feet, 6 feet to 7 feet, 7 feet to 8 feet, 8 feet to9 feet, 9 feet to 10 feet, 10 feet to 11 feet, 11 feet to 12 feet, 12feet to 13 feet, 13 feet to 14 feet, 14 feet to 15 feet, 15 feet to 16feet, 16 feet to 17 feet, 17 feet to 18 feet, 18 feet to 19 feet, or 19feet to 20 feet.

FIG. 3′ shows the first vertically stacked system (1500*) and a secondvertically stacked system (1500′*) contained within an enclosure (ENC*)having an interior (ENC1*). In embodiments, the enclosure may be an areathat is sealed off with an artificial or natural barrier. Inembodiments, the enclosure may be a building, or a structure with a roofand walls. In embodiments, the enclosure may be a shipping containerconforming to the International Organization for Standardization (ISO)specifications. FIG. 3′ shows the enclosure (ENC*) having a first sidewall (1W*), second side wall (2W*), top (5W*), and a floor (1FL*). Forcompleteness, FIG. 4A′ shows the enclosure (ENC*) of FIG. 3′ with athird side wall (3W*) and a fourth side wall (4W*).

In embodiments, the top (5W*), may be comprised of one or more from thegroup consisting of thatch, overlapping layers, shingles, ceramic tiles,membrane, fabric, plastic, metal, concrete, cement, solar panels, wood,a membrane, tar paper, shale, tile, asphalt, polycarbonate, plastic,cement, and composite materials.

In embodiments, one or more solar panels (SOLAR*, SOLAR″*) may bepositioned on top (5W*) of the enclosure (ENC*) may be used to provideelectricity for the farming superstructure system (FSS). In embodiments,one or more solar panels (SOLAR-1W*, SOLAR-2W*, SOLAR-3W*, SOLAR-4W*)may be positioned on one or more walls (1W*, 2W*, 3W*, 4W*) of theenclosure (ENC*) may be used to provide electricity for the farmingsuperstructure system (FSS). In embodiments, one or more solar panels(SOLAR-X*) not positioned on the top (5W*) one or more walls (1W*, 2W*,3W*, 4W*) of the enclosure (ENC*) may be used to provide electricity forthe farming superstructure system (FSS).

In embodiments, electricity from at least one of the solar panels(SOLAR′*, SOLAR″*, (SOLAR-1W*, SOLAR-2W*, SOLAR-3W*, SOLAR-4W*,SOLAR-X*) may be used to provide electricity for one or more from thegroup consisting of: any motor within the farming superstructure system(FSS); any controller within the farming superstructure system (FSS);any conveyor within the farming superstructure system (FSS); a firstplurality of lights (L1*) in the first growing assembly (100*); a firstplurality of light emitting diodes (LED*) in the first growing assembly(100*); a second plurality of lights (L2*) in the second growingassembly (200*); a second plurality of light emitting diodes (LED′*) inthe second growing assembly (200*); blue LEDs (BLED*) within the firstgrowing assembly (100*); red LEDS (RLED*) within the first growingassembly (100*); green LEDS (GLED*) within the first growing assembly(100*); blue LEDs (BLED′*) within the second growing assembly (200*);red LEDS (RLED′*) within the second growing assembly (200*); and greenLEDS (GLED′*) within the second growing assembly (200*). In embodiment,blue lights are positioned within the first growing assembly (100*); redlights are positioned within the first growing assembly (100*); greenlights are positioned within the first growing assembly (100*); bluelights are positioned within the second growing assembly (200*); redlights are positioned within the second growing assembly (200*); andgreen lights are positioned within the second growing assembly (200*).

In embodiments, the walls (1W*, 2W*, 3W*, 4W*) may be comprised of oneor more from the group consisting of metal, concrete, cement, wood,plastic, brick, stone, composite materials, insulation, rockwool,mineral wool, fiberglass, clay, and ceramic. In embodiments, the top(5W*) and walls (1W*, 2W*, 3W*, 4W*) may form one unitary structure suchas a dome, semi-spherical shape, semi-cylindrical, or a greenhouse. Inembodiments, the top (5W*) and walls (1W*, 2W*, 3W*, 4W*) may be clear,translucent, transparent, or not clear.

In embodiments, a plurality of mirrors (MIRROR1, MIRROR2, MIRROR3,MIRROR4, MIRROR5, MIRROR6) are positioned within the interior (ENCL*) ofthe enclosure (ENC*). In embodiments, the plurality of mirrors (MIRROR1,MIRROR2, MIRROR3, MIRROR4, MIRROR5, MIRROR6) reflect light onto theplurality of plants (107*, 207*). In embodiments, the plurality ofmirrors (MIRROR1, MIRROR2, MIRROR3, MIRROR4, MIRROR5, MIRROR6) reflectlight onto the plurality of plants (107*, 207*) wherein the light isprovided by the plurality of lights (L1*, L2*). In embodiments, theplurality of mirrors (MIRROR1, MIRROR2, MIRROR3, MIRROR4, MIRROR5,MIRROR6) reflect light onto the plurality of plants (107*, 207*) whereinthe light is not provided by the plurality of lights (L1*, L2*). Inembodiments, the plurality of mirrors (MIRROR1, MIRROR2, MIRROR3,MIRROR4, MIRROR5, MIRROR6) reflect light onto the plurality of plants(107*, 207*) wherein the light includes sunlight that is directed to theinterior (ENCL*) of the enclosure (ENC*) by the plurality of mirrors(MIRROR1, MIRROR2, MIRROR3, MIRROR4, MIRROR5, MIRROR6).

In embodiments, the plurality of mirrors (MIRROR3, MIRROR4) includes aplurality of mirrors (MIRROR3, MIRROR4) located above the plants toreflect light vertically down onto the plants. In embodiments, theplurality of mirrors (MIRROR1, MIRROR2) includes a plurality of mirrors(MIRROR1, MIRROR2) located on the side of the plants to reflect lightdown horizontally the plants. In embodiments, the plurality of mirrors(MIRROR5, MIRROR6) includes a plurality of mirrors (MIRROR5, MIRROR6)located below the plants to reflect light vertically up onto the plants.

FIG. 4A′

FIG. 4A′ depicts one non-limiting embodiment of FIG. 3′ wherein theenclosure (ENC*) is provided with a temperature control unit (TCU*)including an air heat exchanger (HXA*) that is configured to provide atemperature and/or humidity controlled air supply (Q3*) to the interior(ENC1*) of the enclosure (ENC*) which contains a plurality of verticallystacked systems (1500*, 1500′*).

The interior (ENC1*) of the enclosure (ENC*) has an enclosuretemperature sensor (QT0*) that is configured to output a signal (QXT0*)to a computer (COMP). The interior (ENC1*) of the enclosure (ENC*) hasan enclosure humidity sensor (QH0*) that is configured to output asignal (QXHO*) to a computer (COMP). An air input (Q1*) is configured topermit an air supply (Q3*) to be transferred to the interior (ENC1*) ofthe enclosure (ENC*) via an air supply entry conduit (Q2*). An optionalinlet distributor (Q4*) may be positioned to be in fluid communicationwith the air supply entry conduit (Q2*) to distribute the air supply(Q3*) within the interior (ENC1*) of enclosure (ENC*). In embodiments,the air heater (HXA*) provides a heated air supply (Q3*) to the interior(ENC1*) of the enclosure (ENC*) via said air supply entry conduit (Q2*)and said air input (Q1*). In embodiments, the air heater (HXA*) providesa cooled air supply (Q3*) to the interior (ENC1*) of the enclosure(ENC*) via said air supply entry conduit (Q2*) and said air input (Q1*).

FIG. 4A′ shows a temperature control unit (TCU*) including an air supplyfan (Q12*) and air heater (HXA*) integrated with the interior (ENC1*) ofthe enclosure (ENC*). The air supply fan (Q12*) is connected to theinterior (ENC1*) of the enclosure (ENC*) via the air supply entryconduit (Q2*). The air supply fan (Q12*) is equipped with an air supplyfan motor (Q13*) and controller (Q14*) is configured to input and outputa signal (Q15*) to the computer (COMP). An air heater (HXA*) may beinterposed in the air supply entry conduit (Q2*) in between the airsupply fan (Q12*) and the enclosure (ENC*). In embodiments, the airheater (HXA*) may be interposed in the air supply entry conduit (Q2*) inbetween the enclosure (ENC*) and the air supply fan (Q12*) andinterposed on the air discharge exit conduit (Q23*).

Water (Q16*) in the form of liquid or vapor may be introduced to the airsupply entry conduit (Q2*) via a water transfer conduit (Q17*). A waterinput valve (Q18*), and a water flow sensor (Q19*) may also be installedon the water transfer conduit (Q17*). The water flow sensor (Q19*) isconfigured to input a signal (Q20*) to the computer (COMP).

The air supply (Q3*) may be mixed with the water (Q16*) in a water andgas mixing section (Q21*) of the air supply entry conduit (Q2*). FIG.4A′ shows the water and gas mixing section (Q21*) upstream of the airheater (HXA*) but it may alternately also be placed downstream. The airheater (HXA*) may be electric, operated by natural gas, combustion,solar energy, fuel cell, heat pipes, or it may be a heat transfer devicethat uses a working heat transfer medium, such as steam, or any otherheat transfer medium known to persons having an ordinary skill in theart to which it pertains.

FIG. 4A′ shows the air heater (HXA*) to have a heat transfer mediuminput (Q5*) and a heat transfer medium output (Q6*). In embodiments,heat transfer medium input (Q5*) of the air heater (HXA*) is equippedwith a heat exchanger heat transfer medium inlet temperature (QT3*) thatis configured to input a signal (QXT3*) to the computer (COMP). Inembodiments, heat transfer medium output (Q6*) of the air heater (HXA*)is equipped with a heat exchanger heat transfer medium outlettemperature (QT4*) that is configured to input a signal (QXT4*) to thecomputer (COMP).

A first humidity sensor (Q8*) is positioned on the discharge of the airsupply fan (Q12*) upstream of the water and gas mixing section (Q21*).The first humidity sensor (Q8*) is configured to input a signal (Q9*) tothe computer (COMP*). A heat exchanger inlet gas temperature sensor(QT1*) may be positioned on the discharge of the air supply fan (Q12*)upstream of the air heater (HXA*). The heat exchanger inlet gastemperature sensor (QT1*) is configured to input a signal (QXT1*) to thecomputer (COMP).

A second humidity sensor (Q10*) is positioned on the discharge of theair heater (HXA*) upstream of the air input (Q1*) to the interior(ENC1*) of the enclosure (ENC*). The second humidity sensor (Q10*) isconfigured to input a signal (Q11*) to the computer (COMP*). A heatexchanger outlet gas temperature sensor (QT2*) is positioned on thedischarge of the air heater (HXA*) upstream of the air input (Q1*) tothe interior (ENC1*) of the enclosure (ENC*). The heat exchanger outletgas temperature sensor (QT2*) is configured to input a signal (QXT2*) tothe computer (COMP).

In embodiments, the air supply fan (Q12*), air heater (HXA*), and airsupply (Q2*), permit computer automation while integrated with the heatexchanger inlet gas temperature sensor (QT1*), heat exchanger outlet gastemperature sensor (QT2*), and enclosure temperature sensor (QT0*), tooperate under a wide variety of automated temperature operatingconditions including varying the temperature range in the interior(ENC1*) of the enclosure (ENC*) from between 30 degrees to 90 degreesFahrenheit. In embodiments, the interior (ENC1*) of the enclosure (ENC*)may be maintained within a temperature ranging from between 65 degreesFahrenheit to 85 degrees Fahrenheit. In embodiments, the interior(ENC1*) of the enclosure (ENC*) may be maintained within a temperatureranging from between 60 degrees Fahrenheit to 90 degrees Fahrenheit.

In embodiments, the interior (ENC1*) of the enclosure (ENC*) may bemaintained at a pre-determined temperature ranging from between one ormore from the group selected from 60 degrees Fahrenheit to 61 degreesFahrenheit, 61 degrees Fahrenheit to 62 degrees Fahrenheit, 62 degreesFahrenheit to 63 degrees Fahrenheit, 63 degrees Fahrenheit to 64 degreesFahrenheit, 64 degrees Fahrenheit to 65 degrees Fahrenheit, 65 degreesFahrenheit to 66 degrees Fahrenheit, 66 degrees Fahrenheit to 67 degreesFahrenheit, 67 degrees Fahrenheit to 68 degrees Fahrenheit, 68 degreesFahrenheit to 69 degrees Fahrenheit, 69 degrees Fahrenheit to 70 degreesFahrenheit, 70 degrees Fahrenheit to 71 degrees Fahrenheit, 71 degreesFahrenheit to 72 degrees Fahrenheit, 72 degrees Fahrenheit to 73 degreesFahrenheit, 73 degrees Fahrenheit to 74 degrees Fahrenheit, 74 degreesFahrenheit to 75 degrees Fahrenheit, 75 degrees Fahrenheit to 76 degreesFahrenheit, 76 degrees Fahrenheit to 77 degrees Fahrenheit, 77 degreesFahrenheit to 78 degrees Fahrenheit, 78 degrees Fahrenheit to 79 degreesFahrenheit, 79 degrees Fahrenheit to 80 degrees Fahrenheit, 80 degreesFahrenheit to 81 degrees Fahrenheit, 81 degrees Fahrenheit to 82 degreesFahrenheit, 82 degrees Fahrenheit to 83 degrees Fahrenheit, 83 degreesFahrenheit to 84 degrees Fahrenheit, 84 degrees Fahrenheit to 85 degreesFahrenheit, 85 degrees Fahrenheit to 86 degrees Fahrenheit, 86 degreesFahrenheit to 87 degrees Fahrenheit, 87 degrees Fahrenheit to 88 degreesFahrenheit, 88 degrees Fahrenheit to 89 degrees Fahrenheit, 89 degreesFahrenheit to 90 degrees Fahrenheit, 90 degrees Fahrenheit to 91 degreesFahrenheit, 91 degrees Fahrenheit to 92 degrees Fahrenheit, 92 degreesFahrenheit to 93 degrees Fahrenheit, 93 degrees Fahrenheit to 94 degreesFahrenheit, and 94 degrees Fahrenheit to 95 degrees Fahrenheit.

In embodiments, the air supply fan (Q12*), air heater (HXA*), air supply(Q2*), and water (Q17*) permit the computer automation while integratedwith the first humidity sensor (Q8*), second humidity sensor (Q10*), andenclosure humidity sensor (QH0*), to operate under a wide variety ofautomated operating humidity conditions including varying the humidityrange in the growing assembly (100*, 200*) from between 5 percenthumidity to 100 percent humidity. In embodiments, it is preferred tooperate from between 25 percent humidity to 75 percent humidity. Inembodiments, it is preferred to operate from between 40 percent humidityto 60 percent humidity. In embodiments, it is preferred to operate frombetween 44 percent humidity to 46 percent humidity. In embodiments, itis preferred to operate from between 36 percent humidity to 38 percenthumidity, 38 percent humidity to 40 percent humidity, 40 percenthumidity to 42 percent humidity, 42 percent humidity to 44 percenthumidity, 44 percent humidity to 46 percent humidity, 46 percenthumidity to 48 percent humidity, 48 percent humidity to 50 percenthumidity, 50 percent humidity to 52 percent humidity, 52 percenthumidity to 54 percent humidity, 54 percent humidity to 56 percenthumidity, 56 percent humidity to 58 percent humidity, 58 percenthumidity to 60 percent humidity, 60 percent humidity to 62 percenthumidity, 62 percent humidity to 64 percent humidity, 64 percenthumidity to 66 percent humidity, 66 percent humidity to 68 percenthumidity, or 68 percent humidity to 70 percent humidity.

In embodiments, the air supply fan (Q12*) accepts an air supply (Q3*)from the interior (ENC1*) of the enclosure (ENC*) via an air dischargeexit conduit (Q23*). The air discharge exit conduit (Q23*) is connectedat one end to the enclosure (ENC*) via an air output (Q22*) and atanother end to the air supply fan (Q12*). An air filter (Q24*) may beinstalled on the air discharge exit conduit (Q23*) in between theenclosure (ENC*) and the air supply fan (Q12*) to remove particles priorto entering the air supply fan (Q12*) for recycle back to the enclosure(ENC*). In embodiments, the air filter (Q24*) filters out particulatesfrom the interior (ENC1*) of the enclosure (ENC*) and the air supply fan(Q12*) recycles the filtered air back to the interior (ENC1*) of theenclosure (ENC*). The filtered air may be cooled or heated prior tobeing recycled to the interior (ENC1*) of the enclosure (ENC*).

In embodiments, the air heater (HXA*) adds heat to the interior (ENC1*)of the enclosure (ENC*). In embodiments, the air heater (HXA*) removesheat from the interior (ENC1*) of the enclosure (ENC*) and as a resultmay condense water from the air supply (Q3*) provided from the from theinterior (ENC1*) of the enclosure (ENC*). In embodiments, where the airheater (HXA*) removes heat from the interior (ENC1*) of the enclosure(ENC*) water is collected in the form of condensate (Q25*). Inembodiments, the condensate (Q25*) may in turn be provided to theenclosure (ENC*) via an enclosure condensate input (Q26*) and acondensate conduit (Q27*). The condensate (Q25*) provided to theenclosure (ENC*) via an enclosure condensate input (Q26*) may beprovided to at least one common reservoir (500*, 500′*) via a commontank condensate input (Q28*). In embodiments, the condensate (Q25*) maycontain undesirable compounds (especially viruses and/or bacteria) andin turn may be provided to the input to the first water treatment unit(A1*) as shown in FIG. 10′ as a first undesirable compounds-ladencondensate (Q29*).

FIG. 4B′

FIG. 4B′ depicts one non-limiting embodiment of FIG. 1B′ and FIG. 4A′wherein the enclosure (ENC*) is provided with a temperature control unit(TCU*) including an air heat exchanger (HXA*) that is configured toprovide a temperature and/or humidity controlled air supply (Q3*) to theinterior (ENC1*) of the enclosure (ENC*) which contains a plurality ofgrowing assemblies (100*, 200*).

In embodiments, a fire protection system (FPS*) is contained within theinterior (ENC1*) of the enclosure (ENC*). In embodiments, the fireprotection system (FPS*) includes a sprinkler system (SS-1*). Inembodiments, the sprinkler system (SS-1*) includes a water distributionheader (WDH*) connected to a plurality of spray nozzles (SN-1*, SN-2*,SN-3*). A source of pressurized water (WS-1*) is provided to the waterdistribution header (WDH*). In embodiments, at least a portion of thewater distribution header (WDH*) is a pipe that is made of metal orpolyvinyl chloride. In embodiments, at least a portion of the waterdistribution header (WDH*) has a diameter than includes one or more fromthe group consisting of: 1 inch to 2 inches, 2 inches to 3 inches, 3inches to 4 inches, 4 inches to 5 inches, 5 inches to 6 inches, 6 inchesto 8 inches, and 8 inches to 10 inches.

In embodiments, each of the plurality of spray nozzles (SN-1*, SN-2*,SN-3*) is equipped with an automatic fire sprinkler switch (AFSS-1*,AFSS-2*, AFSS-3*) that permits pressurized water (WS-1*) to pass throughthe plurality of spray nozzles (SN-1*, SN-2*, SN-3*) when there is afire detected within the interior (ENC1*) of the enclosure (ENC*). Inembodiments, the pressure drop of the pressurized water (WS-1*) thatpasses through the plurality of spray nozzles (SN-1*, SN-2*, SN-3*)ranges from: 15 PSI to 25 PSI, 25 PSI to 35 PSI, 35 PSI to 45 PSI, 45PSI to 55 PSI, 55 PSI to 65 PSI, 65 PSI to 75 PSI, 75 PSI to 85 PSI, 85PSI to 95 PSI, 95 PSI to 100 PSI, 100 PSI to 150 PSI, and 150 PSI to 300PSI. In embodiments, the fire protection system (FPS*) includes a smokedetector (SD-1*) that is configured to output a signal (SD-1X*) to acomputer (COMP) in the event of a fire within the interior (ENC1*) ofthe enclosure (ENC*).

In embodiments, the fire protection system (FPS*) is provided with apump (FPS-P*) that is configured to provide a source of pressurizedwater (WS-1*) is provided to the water distribution header (WDH*). Thepump (FPS-P*) is configured to accept and pressurize a source of water(WS-1′*) to form the source of pressurized water (WS-1*) that isprovided to the water distribution header (WDH*) and to the plurality ofspray nozzles (SN-1*, SN-2*, SN-3*). In embodiments, the pump (FPS-P*)is comprised of one of more from the group consisting of a centrifugalpump or a positive displacement pump. In embodiments, the pump is notneeded to provide a source of pressurized water (WS-1*) that is providedto the water distribution header (WDH*) and to the plurality of spraynozzles (SN-1*, SN-2*, SN-3*). In embodiments, a pump discharge pressuresensor (PDPS*) and a pump suction pressure (PSPS*) are equipped tomeasure the pressure at the pump discharge and pump suction,respectively.

In embodiments, a fire protection system (FPS*) is contained within theinterior (ENC1*) of the enclosure (ENC*). In embodiments, cannabisheating, trimming, grinding, volatiles separation, cooling, filtering,evaporating, emulsion mixing, softgel production, as shown in Volume IIare all positioned within the interior (ENC1*) of the enclosure (ENC*)for the fire protection system (FPS*) to protect against. Inembodiments, the interior (ENC1*) of the enclosure (ENC*) is a Class I,Division 1 and 2 classification. In embodiments, the interior (ENC1*) ofthe enclosure (ENC*) is a Class I location because of the consist ofareas where gases, vapors or liquids may exist that have the potentialto become flammable or ignitable, such as first and/or second solvents(SOLV1*, SOLV2*). In embodiments, the interior (ENC1*) of the enclosure(ENC*) is two different divisions in Class I, Division 1 and Division 2,along with three Zones; Zone 0, 1 & 2. Division 1 is a subset of Class Iand is classified as an area where the explosive or flammable gases,vapors or liquids mentioned above can exist under normal, everydayoperating conditions of cannabinoid extraction and evaporation portionsof the FSS. Division 2 is also a subset of Class I and is classified asan area where the explosive or flammable gases, vapors or liquidsmentioned above are not likely to exist during regular operation of thecannabinoid extraction and evaporation portions of the FSS. Inembodiments, the interior (ENC1*) of the enclosure (ENC*) is deemed aZone 0 classification due to the presence of explosive or flammablegases, vapors or liquids for long periods of time during operatingconditions or during a large portion of the operating conditions. Inembodiments, the interior (ENC1*) of the enclosure (ENC*) is deemed aZone 1 classification is described as the presence of explosive orflammable gases, vapors or liquids (e.g.—first and/or second solvents(SOLV1*, SOLV2*)) for some of the time during normal operatingconditions of at least the of the cannabinoid extraction and evaporationportions of the FSS. In embodiments, the interior (ENC1*) of theenclosure (ENC*) is deemed a Zone 2 classification is described as therenot being a likelihood of explosive or flammable gases, vapors orliquids (e.g.—first and/or second solvents (SOLV1*, SOLV2*)) presentduring normal operating conditions. Since the interior (ENC1*) of theenclosure (ENC*) since it is a Class I, Division 1 and 2 classification,explosion-proof equipment, valves, controllers, pumps, heaters, chiller,filters, vacuum systems, evaporation equipment, grinders, humidity andtemperature control systems, flow meters, mixers, sensors, and all otherassets described in Volume II.

In embodiments, the fire protection system (FPS*) includes one or morefire protection systems selected from the group consisting of a drychemical fire suppression system, a dry pipe system, a foam firesuppression system, a gaseous fire suppression system, or a wet firesprinkler system. In embodiments, the fire protection system (FPS*) mayinclude more than one fire protection system. In embodiments, the fireprotection system (FPS*) includes two or more fire protection systemsselected from the group consisting of a dry chemical fire suppressionsystem, a dry pipe system, a foam fire suppression system, a gaseousfire suppression system, or a wet fire sprinkler system. In embodiments,the dry chemical fire suppression system includes pressured drychemicals. In embodiments, the dry pipe system includes automaticsprinklers attached to a piping system containing air or nitrogen underpressure. In embodiments, the foam fire suppression systems includes theuse of a foam extinguishing systems are effective for rapidlycontrolling and extinguishing flammable liquid fires. In embodiments,the gaseous fire suppression systems includes use of carbon dioxide toas a fire-extinguishing agent. In embodiments, the wet fire sprinklersystems includes automatic sprinklers attached to a piping systemconnected to a water supply.

FIG. 5A′

FIG. 5A′ depicts one non-limiting embodiment of FIG. 4A′ wherein thetemperature control unit (TCU*) of FIG. 4A′ is contained within theinterior (ENC1*) of the enclosure (ENC*) and coupled with a humiditycontrol unit (HCU*),

FIG. 5A′ shows the temperature control unit (TCU*) of FIG. 4A′ butcontained within the interior (ENC1*) of the enclosure (ENC*). FIG. 5A′also shows a non-limiting embodiment of a humidity control unit (HCU*)positioned within the interior (ENC1*) of the enclosure (ENC*). Aportion of the humidity control unit (HCU*) may be positioned exteriorto the enclosure (ENC*) and not positioned within the interior (ENC1*).In embodiments, the humidity control unit (HCU*) may also be considereda temperature control unit (TCU*). In embodiments, the humidity controlunit (HCU*) may also be considered a temperature control unit (TCU*)since it may be used to regulate the temperature within the interior(ENC1*) an enclosure (ENC*) wherein a plurality of growing assemblies(100*, 200*) are positioned within the interior (ENC1*) of the enclosure(ENC*).

In embodiments, the humidity control unit (HCU*) may include acompressor (Q30*), a condenser (Q32*), a metering device (Q33*), anevaporator (Q34*), and a fan (Q35*). The fan (Q35*) may be equipped witha motor (Q36*) and a controller (Q37*) that is configured to input oroutput a signal (Q38*) to a computer (COMP).

The compressor (Q31*) is connected to the condenser (Q32*), thecondenser (Q32*) is connected to the metering device (Q33*), themetering device (Q33*) is connected to an evaporator (Q34*), and theevaporator (Q34*) is connected to the compressor (Q31*) to form aclosed-loop refrigeration circuit configured to contain a refrigerant(Q31*). The metering device (Q33*) includes one or more from the groupconsisting of a restriction, orifice, valve, tube, capillary, andcapillary tube. The refrigerant (Q31*) is conveyed from the compressorto the condenser, from the condenser to the evaporator through themetering device, and from the evaporator to the compressor. Theevaporator (Q34*) is positioned within the interior (ENC1*) of theenclosure (ENC*) and is configured to evaporate refrigerant (Q31*)within the evaporator (Q34*) by removing heat from the interior (ENC1*)of the enclosure (ENC*). In embodiments, the evaporator (Q34*) iscontained within the interior (ENC1*) of the enclosure (ENC*). Inembodiments, the condenser (Q32*) is not contained within the interior(ENC1*) of the enclosure (ENC*). The fan (Q35*) is configured to blowair from within the interior (ENC1*) of the enclosure (ENC*) over atleast a portion of the humidity control unit (HCU*).

The humidity control unit (HCU*) is configured to selectively operatethe system in a plurality of modes of operation, the modes of operationincluding at least:

(1) a first mode of operation in which compression of a refrigerant(Q31*) takes place within the compressor (Q30*), and the refrigerant(Q31*) leaves the compressor (Q30*) as a superheated vapor at atemperature greater than the condensation temperature of the refrigerant(Q31*);

(2) a second mode of operation in which condensation of refrigerant(Q31*) takes place within the condenser (Q32*), heat is rejected and therefrigerant (Q31*) condenses from a superheated vapor into a liquid, andthe liquid is cooled to a temperature below the boiling temperature ofthe refrigerant (Q31*); and

(3) a third mode of operation in which evaporation of the refrigerant(Q31*) takes place, and the liquid phase refrigerant (Q31*) boils in theevaporator (Q34*) to form a vapor or a superheated vapor while absorbingheat from the interior (ENC1*) of the enclosure (ENC*).

The evaporator (Q34*) is configured to evaporate the refrigerant (Q31*)to absorb heat from the interior (ENC1*) of an enclosure (ENC*). As aresult, the evaporator (Q34*) may condense water from the interior(ENC1*) of the enclosure (ENC*). In embodiments, the water condensed bythe evaporator (Q34*) contains bacteria. In embodiments, the evaporator(Q34*) condenses water vapor from the interior (ENC1*) of an enclosure(ENC*) and forms condensate (Q39*). In embodiments, the condensate(Q39*) may contain undesirable compounds (especially viruses and/orbacteria) and in turn may be provided to the input to the first watertreatment unit (A1*) as shown in FIG. 10′ as a second undesirablecompounds-laden condensate (Q40*).

FIG. 5B′

FIG. 5B′ depicts one non-limiting embodiment of FIG. 4B′ and FIG. 5A′wherein the temperature control unit (TCU*) of FIG. 4B′ is containedwithin the interior (ENC1*) of the enclosure (ENC*) and coupled with ahumidity control unit (HCU*).

FIG. 5C′

FIG. 5C′ shows one non-limiting embodiment where the compressor (Q30*)within the humidity control unit (HCU*) is that of a thermal compressor(Q30*) that accepts a source of steam. The thermal compressor (Q30*)accepts a steam supply (LDS*) that is provided from FIG. 17F′. Alsoshown is in the thermal compressor (Q30*) discharging condensate (LJC*)to the condensate tank (LAP*) shown on FIG. 17F′.

FIG. 5D′

FIG. 5D′ shows one non-limiting embodiment where the compressor (Q30*)within the humidity control unit (HCU*) is that of a thermal compressor(Q30*) that accepts a source of steam. The thermal compressor (Q30*)accepts a tenth steam supply (LDS*) that is provided from FIG. 17F′.Also shown is in the thermal compressor (Q30*) discharging a tenthcondensate (LJC*) to the condensate tank (LAP*) shown on FIG. 17F′.

In embodiments, the thermal compressor (Q30*) includes a generator(Q50*) and an absorber (Q60*). The first steam supply (LDS*), from FIG.17F′, is transferred from the steam distribution header (LCJ*) and intothe generator (Q50*) of the thermal compressor (Q30*). In embodiments, apump (Q45*) connects the generator (Q50*) to the absorber (Q60*). Also,in embodiments, a metering device (Q55*) is positioned in between theabsorber (Q60*) to the generator (Q50*). The metering device (Q55*) mayinclude one or more from the group consisting of a restriction, orifice,valve, tube, capillary, and capillary tube.

Vapor-phase refrigerant is transferred from the evaporator (Q34*) to theabsorber (Q60*). The refrigerant transferred from the evaporator (Q34*)to the absorber (Q60*) is then absorbed by an absorbent within theabsorber (Q60*). In embodiments, the refrigerant includes water orammonia. In embodiments, the absorbent includes lithium bromine orwater.

A mixture of refrigerant and absorbent is transferred from the absorber(Q60*) to the generator (Q50*) via the pump (Q45*). Heat in the form ofsteam (LDS*) is transferred to the mixture of refrigerant and absorbentwithin the generator (Q50*) to vaporize the refrigerant. Thevapor-phase, or superheated vapor, refrigerant is transferred from thegenerator (Q50*) to the condenser (Q32*). The absorbent is transferredback to the absorber (Q60*) from the generator (Q50*) through themetering device (Q55*). In embodiments, the absorbent that istransferred through the metering device (Q55*) takes a pressure drop. Inembodiments, the generator (Q50*) operates at a pressure that is greaterthan the pressure within the absorber (Q60*).

In embodiments, the thermal compressor (Q30*) may also be called anabsorption chiller. In embodiments, the thermal compressor may have onestage. In embodiments, the thermal compressor may have two stages. Inembodiments, electricity is required to power the pump (Q54*). Inembodiments, the electricity that is required to power the pump (Q54*)comes from the generator (LFH*) shown in FIG. 17F′.

FIG. 5E′

FIG. 5E′ elaborates upon FIG. 5D′ and shows one non-limiting embodimentwhere the compressor (Q30*) within the humidity control unit (HCU*) isthat of a thermal compressor (Q30*) that accepts a source of heat, suchas flue gas (FG1*).

FIG. 6′

FIG. 6′ shows a front view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

FIG. 6′ shows a portion of the farming superstructure system (FSS)including a front view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

The front view shows four growing assemblies (100*, 100′*, 200*, 200′*)including two first growing assemblies (100*, 100′*) and two secondgrowing assembly (200*, 200′*) contained within an interior (ENC1*) ofan enclosure (ENC*). FIG. 6′ shows the two first growing assemblies(100*, 100′*) and two second growing assembly (200*, 200′*) eachequipped with drain ports (110*, 110′*) and drain conduits (111*, 111′*)for draining liquid from each growing assembly (100*, 100′*, 200*,200′*) into a common reservoir (500*) via a common drain conduit (517*)and drain input (518*).

FIG. 6′ shows one pump (P1*) pulling liquid from one common reservoir(500*) and transferring a pressurized liquid through a filter (F1A*)into a plurality of liquid supply headers (300*, 300′*) which are inturn then provided to a plurality of first liquid supply conduits (113*,113′*) and a plurality of second liquid supply conduit (213*, 213′*).Four liquid supply conduits (113*, 113′*, 213*, 213′*) are provided fromtwo liquid supply headers (300*, 300′*) which is provided withpressurized water through one filter (F1A*) by one pump (P1*) pullingliquid from one common reservoir (500*).

The common reservoir (500*) of FIG. 6′ is provided with a pressurizedliquid (29*) through a pressurized liquid transfer conduit (28*) thatenters the common reservoir (500*) via a first water inlet (03*). FIGS.9′ and 10′ describe a liquid distribution module (LDM*) that providesthe pressurized liquid (29*) and transfers it to the plant growingmodule (PGM*) via a pressurized liquid transfer conduit (28*).

As depicted in FIG. 6′ and FIG. 7′, one common reservoir (500*) isprovided for a first vertically stacked system (1500*) and a secondvertically stacked system (1500′*) that contain a total of two firstgrowing assemblies (100*, 100′*) and two second growing assembly (200*,200′*).

The enclosure (ENC*) of FIG. 6′ is shown to have a first side wall(1W*), second side wall (2W*), top (5W*), and A floor (1FL*). Forcompleteness, the top view of the enclosure (ENC*) of FIG. 6′ is shownin FIG. 7′ and is shown to have a first side wall (1W*), second sidewall (2W*), third side wall (3W*), and fourth side wall (4W*).

FIG. 7′

FIG. 7′ shows a top view of one embodiment of a plant growing module(PGM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications.

The enclosure (ENC*) of FIG. 7′ is shown to have a low voltage shut-offswitch (LVV-1*), a humidity control unit (HCU*) (as described in FIG.5′), and a temperature control unit (TCU*) (as described in FIGS. 4A′ &4B′). FIG. 7′ also shows the first vertically stacked system (1500*) andsecond vertically stacked system (1500′*) with one common reservoir(500*). FIG. 7′ also shows a third vertically stacked system (1500″*)and a fourth vertically stacked system (1500′″*) each equipped withtheir own source of pressurized liquid (29C*, 29D*) provided by aplurality of pressurized liquid transfer conduits (28C*, 28D*) asdescribed in detail in FIGS. 9 and 10.

FIG. 8′

FIG. 8′ shows a first side view of one embodiment of a plant growingmodule (PGM*). The enclosure (ENC*) of FIG. 8′ is shown to have ahumidity control unit (HCU*) (as described in FIG. 5′), and atemperature control unit (TCU*) (as described in FIGS. 4A′& 4B′). FIG.8′ shows a first vertically stacked system (1500*) on the left-hand-sideand a second vertically stacked system (1500′*) on the right-hand-side.

The first vertically stacked system (1500*) is shown to have a secondgrowing assembly (200*) located above a first growing assembly (100*).The second growing assembly (200*) has a drain port (210*) and a drainconduit (211*) that directly drains into a common reservoir (500*)located below both growing assemblies (100*, 200*). The drain conduit(211*) from the second growing assembly (200*) is secured to the secondvertical support structure (VSS2*) via a support connection (211X*). Inembodiments, the drain conduit (211*) from the second growing assembly(200*) may be secured to the first vertical support structure (VSS1*),or alternately to the first horizontal support structure (SS1*), orsecond horizontal support structure (SS2*)

The first growing assembly (100*) has a drain port (110*) and a drainconduit (111*) that directly drains into a common reservoir (500*)located below both growing assemblies (100*, 200*). The drain conduit(111*) from the first growing assembly (200*) is secured to the secondvertical support structure (VSS2*) via a support connection (111X*). Inembodiments, the drain conduit (111*) from the first growing assembly(100*) may be secured to the first vertical support structure (VSS1*),or alternately to the first horizontal support structure (SS1*).

The second vertically stacked system (1500′*) is shown to have a secondgrowing assembly (200′*) located above a first growing assembly (100′*).The second growing assembly (200′*) is configured to receive liquid fromthe pump (P1*) via a second liquid supply conduit (213′*) and a liquidinput (214′*). The second liquid supply conduit (213′*) for the secondgrowing assembly (200′*) is secured to the second vertical supportstructure (VSS2′*) via a support connection (213X′*). In embodiments,the second liquid supply conduit (213′*) for the second growing assembly(200′*) may be secured to the first vertical support structure (VSS1′*),or alternately to the first horizontal support structure (SS1′*), orsecond horizontal support structure (SS2′*).

The first growing assembly (100′*) is configured to receive liquid fromthe pump (P1*) via a first liquid supply conduit (113′*) and a liquidinput (114′*). The first liquid supply conduit (113′*) for the firstgrowing assembly (100′*) is secured to the second vertical supportstructure (VSS2′*) via a support connection (113X′*). In embodiments,the first liquid supply conduit (113′*) for the first growing assembly(100′*) may be secured to the first vertical support structure (VSS1′*),or alternately to the first horizontal support structure (SS1′*). Inembodiments, the spacing (1500S*) between the vertically stacked systems(1500*, 1500′*) in FIG. 8′ ranges from 1 foot to 1.5 feet, 1.5 feet to 2feet, 2 feet to 3 feet, 3 feet to 4 feet, 4 feet to 5 feet, 5 feet to 6feet, 6 feet to 7 feet, 7 feet to 8 feet, 8 feet to 10 feet, 10 feet to12 feet, 12 feet to 15 feet, 15 feet to 20 feet In embodiments, thespacing (1500S*) between the vertically stacked systems (1500*, 1500′*)in FIG. 8′ ranges from 2.5 feet to 4.5 feet.

FIG. 9′

FIG. 9′ shows a front view of one embodiment of a liquid distributionmodule (LDM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications andthat is configured to provide a source of liquid to a plurality of plantgrowing modules (PGM*).

FIG. 9′ shows one non-limiting embodiment of a liquid distributionmodule (LDM*) to provide a source of liquid to a plurality of plantgrowing modules (PGM*). The liquid distribution module (LDM*) of FIGS.9′ and 10′ include a first water treatment unit (A1*), a second watertreatment unit (A2*), and a third water treatment unit (A3*), thatprovide a third contaminant depleted water (12*) to the interior (I9*)of a solution tank (18*).

The solution tank (18*) mixes a water supply (01*) with macro-nutrients(601*), micro-nutrients (701*), and/or a pH adjustment solution (801*)to form a mixed solution prior to pumping the mixed solution to at leastone common reservoir (500*) of at least one plant growing modules(PGM*). FIG. 9′ depicts the first water treatment unit (A1*) to includea cation, a second water treatment unit (A2*) to include an anion, and athird water treatment unit (A3*) to include a membrane.

A first water pressure sensor (13*) is positioned on the water inputconduit (14*) that is introduced to the first input (04*) to the firstwater treatment unit (A1*). In embodiments, a filter (y1*), activatedcarbon (y2*), and adsorbent (y3*), are positioned on the water inputconduit (14*) prior to introducing the water supply (01*) to the firstwater treatment unit (A1*). The water supply (01*) may be considered acontaminant-laden water (15*) that includes positively charged ions,negatively charged ions, and undesirable compounds. A first contaminantdepleted water (06*) is discharged by the first water treatment unit(A1*) by a first output (05*). The first contaminant depleted water(06*) may be a positively charged ion depleted water (06A*). The firstcontaminant depleted water (06*) is then transferred to the second watertreatment unit (A2*) via a second input (07*). A second contaminantdepleted water (09*) is discharged by the second water treatment unit(A2*) by a second output (08*). The second contaminant depleted water(09*) may be a negatively charged ion depleted water (09A*). The secondcontaminant depleted water (09*) is then transferred to the third watertreatment unit (A3*) via a third input (I0*). A third contaminantdepleted water (12*) is discharged by the third water treatment unit(A3*) by a third output (I1*). The third contaminant depleted water(12*) may be an undesirable compounds depleted water (12A*). The thirdcontaminant depleted water (12*) is then transferred to the interior(I9*) of a solution tank (18*) via a water supply conduit (21*) andwater input (20*).

Within the interior (I9*) of the solution tank (18*), the thirdcontaminant depleted water (12*) may be mixed with macro-nutrients(601*) from a macro-nutrient supply tank (600*), micro-nutrients (701*)from a micro-nutrient supply tank (700*), and/or a pH adjustmentsolution (801*) from a micro-nutrient supply tank (700*). Inembodiments, a cation (y4*), an anion (y5*), and a polishing unit (y6*),are positioned on the water supply conduit (21*) in between the thirdwater treatment unit (A3*) and the water input (20*) of the solutiontank (18*). The polishing unit (y6*) may be any type of conceivabledevice to improve the water quality such as an ultraviolet unit, ozoneunit, microwave unit, a distillation system or the like.

In embodiments, water supply valve (16*) is positioned on the watersupply conduit (21*) in between the third water treatment unit (A3*) andthe water input (20*) of the solution tank (18*). The water supply valve(16*) is equipped with a controller (17*) that inputs or outputs asignal from a computer (COMP). In embodiments, the solution tank (18*)is equipped with a high-level sensor (25*) and a low-level sensor (26*).The high-level sensor (25*) is used for detecting a high level and thelow-level sensor (26*) is used for detecting a low level. The high-levelsensor (25*) is configured to output a signal to the computer (COMP)when the high-level sensor (25*) is triggered by a high level of liquidwithin the solution tank (18*). The low-level sensor (26*) is configuredto output a signal to the computer (COMP) when the low-level sensor(26*) is triggered by a low level of liquid within the solution tank(18*). In embodiments, when the low-level sensor (26*) sends a signal tothe computer (COMP), the water supply valve (16*) on the water supplyconduit (21*) is opened and introduces water into the solution tank(18*) until the high-level sensor (25*) is triggered thus sending asignal to the computer (COMP) to close the water supply valve (16*).This level control loop including the high-level sensor (25*) fordetecting a high level and a low-level sensor (26*) for detecting alower level may be coupled to the operation of the water supply valve(16*) for introducing a water supply (01*) through a first watertreatment unit (A1*), a second water treatment unit (A2*), and a thirdwater treatment unit (A3*), to provide a third contaminant depletedwater (12*) to the interior (I9*) of a solution tank (18*). The liquiddistribution module (LDM*) is equipped with a low voltage shut-offswitch (LVV-2*).

The interior (I9*) of the solution tank (18*) is equipped with an oxygenemitter (35*) for oxygenating the water within. The oxygen emitter (35*)is connected to the interior (I9*) of the solution tank (18*) via anoxygen emitter connection (36*) which protrudes the solution tank (18*).The solution tank (18*) may be placed on a load cell (40*) for measuringthe mass of the tank. The solution tank (18*) may be equipped with amixer (38*) for mixing water with macro-nutrients (601*),micro-nutrients (701*), and/or a pH adjustment solution (801*). Themixer (38*) may be of an auger or blade type that is equipped with amotor (39*).

The solution tank (18*) has a water output (22*) that is connected to awater discharge conduit (23*). The water discharge conduit (23*) isconnected at one end to the water output (22*) of the solution tank(18*) and at another end to a water supply pump (24*). The water supplypump (24*) provides a source of pressurized liquid (29*) via apressurized liquid transfer conduit (28*).

A second water pressure sensor (27*) is positioned on the pressurizedliquid transfer conduit (28*). A flow sensor (30*) and a water qualitysensor (33*) may be positioned on the pressurized liquid transferconduit (28*). The water quality sensor (33*) can measure electricalconductivity or resistivity. The pressurized liquid transfer conduit(28*) can be split into a plurality of streams for providing to aplurality of plant growing modules (PGM*) having a plurality of commonreservoirs (500*, 500′*, 500″*, 500′″*).

The pressurized liquid transfer conduit (28*) can be split into aplurality of streams including a first pressurized liquid transferconduit (28A*) for sending to a common tank (500*) for the firstvertically stacked system (1500*) and second vertically stacked system(1500′*) of FIG. 6′, a second pressurized liquid transfer conduit (28B*)as a back-up water source to the common tank (500*) of FIG. 6′, a thirdpressurized liquid transfer conduit (28C*) for the common tank (500″*)for the third vertically stacked system (1500″*) of FIG. 6′, and afourth pressurized liquid transfer conduit (28D*) for the common tank(500′″*) for the fourth vertically stacked system (1500′″*) of FIG. 6′.

FIG. 10′

FIG. 10′ shows a top view of one embodiment of a liquid distributionmodule (LDM*) provided inside of a shipping container conforming to theInternational Organization for Standardization (ISO) specifications andthat is configured to provide a source of liquid to a plurality of plantgrowing modules (PGM*).

FIG. 11′

FIG. 11′ shows a first side view of one embodiment of a liquiddistribution module (LDM*).

FIG. 12′

FIG. 12′ shows one non-limiting embodiment of a fabric (104*) used in agrowing assembly (100*), the fabric (104*) having a multi-pointtemperature sensor (MPT100*) connected thereto for measuringtemperatures at various lengths along the sensor's length.

FIGS. 12′ and 1′3 disclose a fabric (104*) that includes a multi-pointtemperature sensor (MPT100*). The fabric (104*) may be used in each ofthe growing assemblies (100*, 200*). The fabric has a width (104W*) anda length (104L*). The multi-point temperature sensor (MPT100*) isconnected to the fabric (104*) and is configured to measure thetemperature of the fabric (104*) along several points along the width(104W*).

FIG. 12′ shows the multi-point temperature sensor (MPT100*) having 8temperature sensor elements to measure the temperature across a firstdistance (104W1*), second distance (104W2*), third distance (104W*),fourth distance (104W4*), fifth distance (104W5*), sixth distance(104W6*), seventh distance (104W7*), and eighth distance (104W8*). Inembodiments, each of the 8 temperature sensor elements is configured toinput a signal to the computer (COMP*). The temperature element at thefirst distance (104W1*) sends a first signal (XMPT1*) to a computer(COMP). The temperature element at the second distance (104W2*) sends asecond signal (XMPT2*) to a computer (COMP). The temperature element atthe third distance (104W*) sends a third signal (XMPT3*) to a computer(COMP). The temperature element at the fourth distance (104W4*) sends afourth signal (XMPT4*) to a computer (COMP). The temperature element atthe fifth distance (104W5*) sends a fifth signal (XMPT5*) to a computer(COMP). The temperature element at the sixth distance (104W6*) sends asixth signal (XMPT6*) to a computer (COMP). The temperature element atthe seventh distance (104W7*) sends a seventh signal (XMPT7*) to acomputer (COMP). The temperature element at the eighth distance (104W8*)sends an eighth signal (XMPT8*) to a computer (COMP). An averagetemperature of the fabric (104*) may be obtained by averaging at leasttwo of the signals from the multi-point temperature sensor (MPT100*).

Each of the distances (104W1*, 104W2*, 104W3*, 104W4*, 104W5*, 104W6*,104W7*, 104W8*) is measured relative to the base width (104W0*) of thefabric (104*). In embodiments, the fabric (104*) is comprised of one ormore from the group consisting of plastic, polyethylene, high-densitypolyethylene (HDPE), low-density polyethylene (LDPE), polyethyleneterephthalate (PET), polyacrylonitrile, and polypropylene.

In embodiments, the fabric (104*) is configured to have a wicking heightconstant characterized by a wicking height range from 0.4 inches to 1.9inches. In embodiments, the fabric (104*) is configured to have awicking height constant characterized by a wicking height range from0.40 inches to 0.45 inches, 0.45 inches to 0.50 inches, 0.50 inches to0.55 inches, 0.55 inches to 0.60 inches, 0.60 inches to 0.65 inches,0.65 inches to 0.70 inches, 0.70 inches to 0.75 inches, 0.75 inches to0.80 inches, 0.80 inches to 0.85 inches, 0.85 inches to 0.90 inches,0.90 inches to 0.95 inches, 0.95 inches to 1.00 inches, 1.00 inches to1.05 inches, 1.05 inches to 1.10 inches, 1.10 inches to 1.15 inches,1.15 inches to 1.20 inches, 1.20 inches to 1.25 inches, 1.25 inches to1.30 inches, 1.30 inches to 1.35 inches, 1.35 inches to 1.40 inches,1.40 inches to 1.45 inches, 1.45 inches to 1.50 inches, 1.50 inches to1.55 inches, 1.55 inches to 1.60 inches, 1.60 inches to 1.65 inches,1.65 inches to 1.70 inches, 1.70 inches to 1.75 inches, 1.75 inches to1.80 inches, 1.80 inches to 1.85 inches, or 1.85 inches to 1.90 inches.

The wicking height constant is a measurement of an ability of the fabric(104) to absorb moisture. In embodiments, the fabric (104) is configuredto have an absorbance constant characterized by an absorbance range from0.001 lb/in² to 0.005 lb/in². In embodiments, the fabric (104) isconfigured to have an absorbance constant characterized by an absorbancerange from 0.0010 lb/in² to 0.0015 lb/in², 0.0015 lb/in² to 0.0020lb/in², 0.0020 lb/in² to 0.0025 lb/in², 0.0025 lb/in² to 0.0030 lb/in²,0.0030 lb/in² to 0.0035 lb/in², 0.0035 lb/in² to 0.0040 lb/in², 0.0040lb/in² to 0.0045 lb/in², or 0.0045 lb/in² to 0.0050 lb/in², or 0.0050lb/in².

In embodiments, the absorbance constant is a measurement of moisture thefabric retains. In embodiments, the moisture that the fabric (104*)retains may be provided by a liquid, mist, spray, water, mixture ofwater with macro-nutrients, micro-nutrients, pH adjustment solution,carbohydrates, enzymes, vitamins, hormones.

FIG. 13′

FIG. 13′ shows another one non-limiting embodiment of a fabric (104*)used in a growing assembly (100*).

FIG. 14′

FIG. 14′ depicts a computer (COMP) that is configured to input and/oroutput signals listed in FIGS. 1-17K′. In embodiments, the computer(COMP) for the Farming Superstructure System (FSS) (disclosed in VolumeII) is the same computer (COMP) used in the Insect ProductionSuperstructure System (IPSS) (disclosed in Volume I). In embodiments,the computer (COMP) for the Farming Superstructure System (FSS)(disclosed in Volume II) is not the same computer (COMP) used in theInsect Production Superstructure System (IPSS) (disclosed in Volume I).

FIG. 15′

FIG. 15′ shows a plurality of cannabis trimmers (TR*, TR**) that areconfigured to trim at least a portion of the cannabis (107*, 207*) thatwas growing in each growing assembly (100*, 200*). FIG. 15′ shows afirst trimmer (TR*) configured to trim at least a portion of thecannabis (107*, 207*) to produce a first trimmed cannabis (TR1*) thatwas growing in each growing assembly (100*, 200*) followed by a secondstage trimmer (TR**) configured to trim at least a portion of thetrimmed cannabis (TR1*) from the first stage trimmer (TR*) to produce asecond trimmed cannabis (TR1**).

Once the cannabis (107*, 207*) is harvested from each growing assembly(100*, 200*), the cannabis (107*, 207*) may be trimmed by use of atleast one trimmer (TR*, TR**). In embodiments, trimming the cannabis(107*, 207*) is necessary to obtain a final product for medicinal orrecreational use. Trimming the cannabis (107*, 207*) may be done forseveral reasons including improving appearance, taste, andtetrahydrocannabinol (THC) concentration.

Cannabis (107*, 207*) consists of the leaves, seeds, stems, roots, orany reproductive structures. In embodiments, the reproductive structuresmay be flower. In embodiments, a flower may be a reproductive structure.In embodiments, the reproductive structures may be buds. In embodiments,a bud may be a reproductive structure. In embodiments, trimming removesat least a portion of the leaves and stems from the reproductivestructures. In embodiments, cannabis (107*, 207*) is harvested from eachgrowing assembly (100*, 200*) by severing the plants with a cuttingtool. In embodiments, the roots of the cannabis (107*, 207*) are notintroduced to the trimmer (TR*). In embodiments, cannabis (107*, 207*)comprising leaves, seeds, stems, and reproductive structures (buds) areintroduced to the trimmer (TR*). In embodiments, cannabis (107*, 207*)comprising leaves, seeds, stems, roots, and reproductive structures(buds) are introduced to the trimmer (TR*).

In embodiments, the first trimmer (TR*) separates the leaves and/orstems from the buds. In embodiments, the first trimmer (TR*) separatesthe buds from the leaves and stems. In embodiments, the first trimmer(TR*) separates the buds from the leaves and stems by applying using arotational motion provided by a first motor (MT1*). In embodiments, thetrimmer (TR*) imparts a rotational motion upon the cannabis (107*,207*). FIG. 15′ displays the trimmer (TR*) accepting a source ofcannabis (107*, 207*) and trims leaves and/or stems from thereproductive structures (buds) to produce trimmed cannabis (TR1*) andfirst trimmings (TR2*). In embodiment, the first trimmer (TR*) rotatesat a revolutions per minute (rpm) including one or more selected fromthe group consisting of 30 rpm to 35 rpm, 35 rpm to 40 rpm, 40 rpm to 45rpm, 45 rpm to 50 rpm, 50 rpm to 55 rpm, 55 rpm to 60 rpm, 60 rpm to 65rpm, 65 rpm to 70 rpm, 70 rpm to 75 rpm, 75 rpm to 80 rpm, 80 rpm to 85rpm, 85 rpm to 90 rpm, 90 rpm to 95 rpm, 95 rpm to 100 rpm, 100 rpm to105 rpm, 105 rpm to 110 rpm, 110 rpm to 115 rpm, 115 rpm to 120 rpm, 120rpm to 125 rpm, 125 rpm to 130 rpm, 130 rpm to 135 rpm, 135 rpm to 140rpm, 140 rpm to 145 rpm, 145 rpm to 150 rpm, 150 rpm to 155 rpm, 155 rpmto 160 rpm, 160 rpm to 165 rpm, 165 rpm to 170 rpm, 170 rpm to 175 rpm,175 rpm to 180 rpm, 180 rpm to 185 rpm, 185 rpm to 190 rpm, 190 rpm to195 rpm, 195 rpm to 200 rpm, 200 rpm to 205 rpm, 205 rpm to 210 rpm, 210rpm to 215 rpm, 215 rpm to 220 rpm, and 220 rpm to 225 rpm.

In embodiments, the first trimmer (TR*) moves the cannabis (107*, 207*)to a second trimmer (TR**) to produce a second trimmed cannabis (TR**).Use of two stages of trimmers (TR*, TR**) increases efficiency of thetrimming process and reduces manual labor in quality control byminimizing hand trimming.

In embodiments, a rotational motion cannabis (107*, 207*) passes thecannabis (107*, 207*) across a first blade (CT2*), the first blade isconfigured to separate the leaves or stems from the buds, to providefirst trimmed cannabis (TR1*) that is depleted of leaves or stems. Inembodiments, the first trimmer (TR*) moves the cannabis (107*, 207*)across a first blade (CT2*), the first blade is configured to separatethe leaves or stems from the buds, to provide trimmed cannabis that isdepleted of leaves or stems.

In embodiments, the second trimmer (TR**) separates the leaves and/orstems from the from the first trimmed cannabis (TR1*). In embodiments,the second trimmer (TR**) separates the buds from the leaves and stemsof the first trimmed cannabis (TR1*) to produce a second trimmedcannabis (TR1**) that has a reduced amount of leaves and/or stemsrelative to the first trimmed cannabis (TR1*). In embodiments, thesecond trimmer (TR**) separates the buds from the leaves from the firsttrimmed cannabis (TR1**) and stems by applying using a rotational motionprovided by a second motor (MT1**). In embodiments, the second motor(MT!*) is not needed since the first motor (MT1*) rotates both the firsttrimmer (TR*) and the second trimmer (TR**).

In embodiments, the second trimmer (TR8*) imparts a rotational motionupon the first trimmed cannabis (TR1*). FIG. 15′ displays the secondtrimmer (TR**) accepting the first trimmed cannabis (TR1*) and trims atleast a portion of the leaves and/or stems therefrom to produce a secondtrimmed cannabis (TR1**) and second trimmings (TR2**). In embodiments, avacuum is pulled on the first trimmings (TR1*) and the second trimmings(TR1**).

In embodiment, the second trimmer (TR**) rotates at a revolutions perminute (rpm) including one or more selected from the group consisting of30 rpm to 35 rpm, 35 rpm to 40 rpm, 40 rpm to 45 rpm, 45 rpm to 50 rpm,50 rpm to 55 rpm, 55 rpm to 60 rpm, 60 rpm to 65 rpm, 65 rpm to 70 rpm,70 rpm to 75 rpm, 75 rpm to 80 rpm, 80 rpm to 85 rpm, 85 rpm to 90 rpm,90 rpm to 95 rpm, 95 rpm to 100 rpm, 100 rpm to 105 rpm, 105 rpm to 110rpm, 110 rpm to 115 rpm, 115 rpm to 120 rpm, 120 rpm to 125 rpm, 125 rpmto 130 rpm, 130 rpm to 135 rpm, 135 rpm to 140 rpm, 140 rpm to 145 rpm,145 rpm to 150 rpm, 150 rpm to 155 rpm, 155 rpm to 160 rpm, 160 rpm to165 rpm, 165 rpm to 170 rpm, 170 rpm to 175 rpm, 175 rpm to 180 rpm, 180rpm to 185 rpm, 185 rpm to 190 rpm, 190 rpm to 195 rpm, 195 rpm to 200rpm, 200 rpm to 205 rpm, 205 rpm to 210 rpm, 210 rpm to 215 rpm, 215 rpmto 220 rpm, and 220 rpm to 225 rpm. In embodiment, the second trimmer(TR**) rotates at a revolutions per minute (rpm) greater than the rpm ofthe first trimmer (TR*). In embodiment, the second trimmer (TR**)rotates at a revolutions per minute (rpm) lesser than the rpm of thefirst trimmer (TR*). In embodiment, the second trimmer (TR**) rotates ata revolutions per minute (rpm) equal to rpm of the first trimmer (TR*).

In embodiments, the second trimmer (TR**) moves the cannabis (107*,207*) from the first trimmer (TR*) to another location. In embodiments,a rotational motion is imparted upon the first trimmed cannabis (TR1*)within the second trimmer (TR**) which passes the first trimmed cannabis(TR1*) across a second blade (CT2**), the second blade is configured toseparate at least a portion of the leaves and/or stems from the firsttrimmed cannabis (TR1*) to provide a second trimmed cannabis (TR1**)that has a reduced amount of leaves and/or stems relative to the firsttrimmed cannabis (TR1*).

In embodiments, the first trimmings (TR2*) include a first gas andtrimmings mixture (GTM2). In embodiments, the second trimmings (TR2**)include a second gas and trimmings mixture (GTM3). In embodiments, thefirst trimmings (TR2*) including the first gas and trimmings mixture(GTM2) are mixed with the second trimmings (TR2**) including the secondgas and trimmings mixture (GTM3) to produce a combined gas and trimmingsmixture (GTM1). The combined gas and trimmings mixture (GTM1) includesthe first trimmings (TR*) and the second trimmings (TR**) and a gas. Inembodiments, the gas includes air, nitrogen, carbon dioxide.

In embodiments, the combined gas and trimmings mixture (GTM1) isintroduced to a cyclone (TRX1). The cyclone (TRX1) is configured toseparate the cannabis trimmings (TR*, TR**) from the combined gas andtrimmings mixture (GTM1) and produce a first separated trimmings (ST**).The first separated trimmings (ST**) is evacuated from the cyclone(TRX1) via a first dipleg (TRX1*). A first trimmings depleted gas(FTDG*) is evacuated from the cyclone (TRx1) and is introduced to afilter (TRX2). In embodiments, insects are present within the cannabisintroduced To the first and/or second trimmer (TR*, TR**). Inembodiments, insects are separated from the trimmings (TR2*, TR2**) withthe cyclone (TRX1) and/or the filter (TRX2).

The filter (TRX2) has a filter element (TRX2*) which is configured toremove additional trimmings from the first trimmings depleted gas(FTDG*) to produce a second trimmings depleted gas (STDG*) which has areduced amount of trimmings relative to the first trimmings depleted gas(FTDG*). In embodiments, the additional trimmings removed from the firsttrimmings depleted gas (FTDG*) within the filter (TRX2) includes secondseparated trimmings (ST***). In embodiments, the first separatedtrimmings (ST**) and the second separated trimmings (ST***) are combinedand send to the grinder (GR*) as shown on FIG. 16′.

The second trimmings depleted gas (STDG*) is evacuated from the filter(TRX2) and is introduced to fan (TRX3). The fan (TRX3) is configured topull a vacuum on the filter (TRX3), the cyclone (TRX1), and the firstand second trimmers (TR*, TR**). In embodiments, the vacuum pulled onthe first and second trimmers (TR*, TR**) pulls the trimmed cannabis(TR1*, TR1**) up against the blades (CT2*, CT2**) within each trimmer(TR*, TR**). The fan (TRX3) is operated by a motor (TRX3). The fan(TRX2) is configured to configured to pull a vacuum on the filter(TRX3), the cyclone (TRX1), and the first and second trimmers (TR*,TR**) by applying a vacuum with a velocity pressure range from: betweenabout 0.001 inches of water to about 0.005 inches of water; betweenabout 0.005 inches of water to about 0.01 inches of water; between about0.01 inches of water to about 0.02 inches of water; between about 0.02inches of water to about 0.03 inches of water; between about 0.03 inchesof water to about 0.04 inches of water; between about 0.04 inches ofwater to about 0.05 inches of water; between about 0.05 inches of waterto about 0.06 inches of water; between about 0.06 inches of water toabout 0.07 inches of water; between about 0.07 inches of water to about0.08 inches of water; between about 0.08 inches of water to about 0.09inches of water; between about 0.09 inches of water to about 0.1 inchesof water; between about 0.1 inches of water to about 0.2 inches ofwater; between about 0.2 inches of water to about 0.3 inches of water;between about 0.3 inches of water to about 0.4 inches of water; betweenabout 0.4 inches of water to about 0.5 inches of water; between about0.5 inches of water to about 0.6 inches of water; between about 0.6inches of water to about 0.7 inches of water; between about 0.7 inchesof water to about 0.8 inches of water; between about 0.8 inches of waterto about 0.9 inches of water; between about 0.9 inches of water to about1 inch of water; between about 1 inch of water to about 1.25 inches ofwater; between about 1.25 inches of water to about 1.5 inches of water;between about 1.5 inches of water to about 2 inches of water; betweenabout 2 inches of water to about 3 inches of water; between about 3inches of water to about 4 inches of water; between about 4 inches ofwater to about 5 inches of water; between about 5 inches of water toabout 6 inches of water; between about 6 inches of water to about 7inches of water; between about 7 inches of water to about 8 inches ofwater; between about 8 inches of water to about 9 inches of water;between about 9 inches of water to about 10 inches of water; betweenabout 10 inch of water to about 15 inches of water; between about 15inches of water to about 25 inches of water; between about 25 inches ofwater to about 50 inches of water; between about 50 inches of water toabout 75 inches of water; between about 75 inches of water to about 100inches of water; between about 100 inches of water to about 150 inchesof water; between about 150 inches of water to about 200 inches ofwater; between about 200 inches of water to about 250 inches of water;between about 250 inches of water to about 300 inches of water; betweenabout 300 inches of water to about 350 inches of water; and, betweenabout 350 inches of water to about 400 inches of water.

Gas is evacuated from the fan (TRX3) where it is then introduced to anadsorbent (TRX4). The adsorbent removes odor from the gas and produces aclean gas (TRX5). The clean gas (TRX5) has a reduced amount of volatileorganic compounds within it relative to the gas that is evacuated fromthe fan (TRX3).

In embodiments, the harvested cannabis removed from the interior of theenclosure is immediately frozen within a freezer. In embodiments, theharvested cannabis removed from the interior of the enclosure isimmediately frozen within a freezer to produce fresh frozen cannabis. Inembodiments, the harvested cannabis removed from the interior of theenclosure is immediately frozen within a cryogenic liquid such as liquidnitrogen, liquid argon, liquid helium, liquid hydrogen, or liquidoxygen. In embodiments, the harvested cannabis removed from the interiorof the enclosure is frozen at a temperature ranging from 32 degreesFahrenheit to 0 degrees Fahrenheit, 0 degrees Fahrenheit to −10 degreesFahrenheit, −10 degrees Fahrenheit to −20 degrees Fahrenheit, −20degrees Fahrenheit to −30 degrees Fahrenheit, −30 degrees Fahrenheit to−40 degrees Fahrenheit, −40 degrees Fahrenheit to −50 degreesFahrenheit, −50 degrees Fahrenheit to −75 degrees Fahrenheit, −75degrees Fahrenheit to −100 degrees Fahrenheit, −100 degrees Fahrenheitto −125 degrees Fahrenheit, −135 degrees Fahrenheit to −150 degreesFahrenheit, −150 degrees Fahrenheit to −250 degrees Fahrenheit, or −250degrees Fahrenheit to −350 Fahrenheit.

In embodiments, the harvested cannabis removed from the interior of theenclosure is frozen immediately after it is harvested within a timeduration after harvesting selected from the time durations inducing 0minutes to 1 minute, 1 minutes to 3 minutes, 3 minutes to 5 minutes, 5minutes to 7 minutes, 7 minutes to 9 minutes, 9 minutes to 11 minutes,11 minutes to 13 minutes, 13 minutes to 15 minutes, 15 minutes to 20minutes, 20 minutes to 25 minutes, 25 minutes to 30 minutes, 30 minutesto 35 minutes, 35 minutes to 40 minutes, 40 minutes to 45 minutes, 45minutes to 50 minutes, 50 minutes to 55 minutes, 55 minutes to 60minutes, 60 minutes to 75 minutes, 75 minutes to 90 minutes, 90 minutesto 105 minutes, or 105 minutes to 120 minutes.

FIG. 16′

FIG. 16′ shows a grinder (GR*) that is configured to grind at least aportion of the cannabis (107*, 207*) that was growing in each growingassembly (100*, 200*). FIG. 16′ also shows a grinder (GR) that isconfigured to grind at least a portion of the trimmed cannabis (TR1*)that was trimmed by the trimmer (TR*) as shown in FIG. 15′.

A grinder (GR*) generates a ground cannabis (GR1*). The grinder may beused to grind (i) a portion of the cannabis (107*, 207*) harvested fromeach growing assembly (100*, 200*) or (ii) a portion of the trimmedcannabis (TR1*) that is trimmed by the trimmer (TR*) to produce groundcannabis (GR1*). In embodiments, grinding of the cannabis is requiredfor creating food products including a multifunctional composition. Inembodiments, the trimmings (TR2*, TR2**) are provided to the grinder(GR*) shown in FIG. 15′.

In embodiments, the trimmings (TR2*) from the first trimmer (TR*) areprovided to the grinder (GR*) shown in FIG. 15′. In embodiments, thetrimmings (TR2**) from the second trimmer (TR**) are provided to thegrinder (GR*) shown in FIG. 15′.

A grinder (GR*) generates a ground cannabis (GR1*) to a size rangingfrom 20 microns to 40 microns, 40 microns to 60 microns, 60 microns to80 microns, 80 microns to 100 microns, 100 microns to 150 microns, 150microns to 200 microns, 200 microns to 250 microns, 250 microns to 300microns, 300 microns to 350 microns, 350 microns to 400 microns, 400microns to 450 microns, 450 microns to 500 microns, 500 microns to 600microns, 600 microns to 700 microns, 700 microns to 800 microns, 800microns to 900 microns, 900 microns to 1000 microns, 1000 microns to1250 microns, 1250 microns to 1500 microns, 1500 microns to 1750microns, 1750 microns to 2000 microns, 2000 microns to 2250 microns,2250 microns to 2500 microns, 2500 microns to 2750 microns, 2750 micronsto 3000 microns, 3000 microns to 3500 microns, 3500 microns to 4000microns, 4000 microns to 4500 microns, 4500 microns to 5000 microns,5000 microns to 5500 microns, 5500 microns to 6000 microns, 6000 micronsto 6500 microns, 6500 microns to 7000 microns, 7000 microns to 7500microns, 7500 microns to 8000 microns, 8000 microns to 8500 microns,8500 microns to 9000 microns, 9000 microns to 9500 microns, 9500 micronsto 10000 microns, 10000 microns to 15000 microns, 15000 microns to 25000microns, or 25000 microns to 35000 microns.

FIG. 17′

FIG. 17′ shows a heater (HTR1*) that is configured to heat at least aportion of Cannabis plants (107*, 207*) that was growing in each growingassembly (100*, 200*). In embodiments, heating the cannabis is requiredfor creating food products including a multifunctional composition.

FIG. 17′ shows a heating unit (HTR1*) that is configured to heat atleast a portion of Cannabis plants (107*, 207*) that was growing in eachgrowing assembly (100*, 200*). FIG. 17′ shows a heater (HTR1*) that isconfigured to heat at least a portion of the cannabis (107*, 207*) thatwas growing in each growing assembly (100*, 200*). FIG. 17′ also shows aheater (HTR1*) that is configured to heat at least a portion of thetrimmed cannabis (TR1*) that was trimmed by the trimmer (TR*) as shownin FIG. 15′. FIG. 17′ also shows a heater (HTR1*) that is configured toheat at least a portion of the ground cannabis (GR1*) that was ground bythe grinder (GR*) as shown in FIG. 16′. The heater (HTR1*) may be usedto heat (i) a portion of the cannabis (107*, 207*) harvested from eachgrowing assembly (100*, 200*), (ii) a portion of the trimmed cannabis(TR1*) that is trimmed by the trimmer (TR*), or (ii) a portion of theground cannabis (GR1*) that is ground by the cannabis (GR1*).

The heater (HTR1*) generates a heated cannabis (HT1*). The heater(HTR1*) is configured to heat the cannabis (107*, 207*). In embodiments,the heater (HTR1*) is configured to heat the cannabis (107*, 207*) asthe cannabis (107*, 207*) passes through the heater (HTR1*) via aconveyor (CVR1*).

In embodiments, heating the cannabis (107*, 207*) removes carbon dioxide(CO2R*) from the cannabis (107*, 207*) to form a carbon dioxide depletedcannabis (CO2-1*). In embodiments, the carbon dioxide depleted cannabis(CO2-1*) is synonymous with the heated cannabis (HT1*).

In embodiments, heating the cannabis (107*, 207*) decarboxylates thecannabis (107*, 207*) to produce a decarboxylated cannabis (DCX*). Inembodiments, heating the cannabis (107*, 207*) decarboxylates thetetrahydrocannabinolic acid (THCA) within the cannabis (107*, 207*) toform active tetrahydrocannabinol. In embodiments, decarboxylation is achemical reaction that removes a carboxyl group and releases carbondioxide (CO2R*). In embodiments, heating the cannabis (107*, 207*)removes carbon dioxide form the cannabis (107*, 207*) to form a carbondioxide depleted cannabis (CO2-1*).

The heater (HTR1*) is equipped with a heater temperature sensor (HTR1T*)that sends a signal (HTR1X*) to the computer (COMP). In embodiments, theheater (HTR1*) is operated within a temperature ranging from 185 degreesF. to 280 degrees F. In embodiments, the heater (HTR1*) is operatedwithin a temperature ranging from 205 degrees F. to 250 degrees F. Inembodiments, the heater (HTR1*) produces a heated cannabis (HT1*) thathas a temperature ranging from 185 degrees F. to 280 degrees F. Inembodiments, the heater (HTR1*) produces a heated cannabis (HT1*) thathas a temperature ranging from 205 degrees F. to 250 degrees F.

In embodiments, the heater (HTR1*) is operated within a temperatureranging from 175 degrees Fahrenheit to 200 degrees Fahrenheit, 200degrees Fahrenheit to 225 degrees Fahrenheit, 225 degrees Fahrenheit to250 degrees Fahrenheit, 250 degrees Fahrenheit to 275 degreesFahrenheit, 275 degrees Fahrenheit to 300 degrees Fahrenheit, 300degrees Fahrenheit to 325 degrees Fahrenheit, 325 degrees Fahrenheit to350 degrees Fahrenheit, 350 degrees Fahrenheit to 375 degreesFahrenheit, 375 degrees Fahrenheit to 400 degrees Fahrenheit, or 400degrees Fahrenheit to 425 degrees Fahrenheit.

In embodiments, the cannabis is dried at a temperature ranging from 50to 60 degrees Fahrenheit, 60 to 65 degrees Fahrenheit, 65 to 70 degreesFahrenheit, 70 to 75 degrees Fahrenheit, 75 to 80 degrees Fahrenheit, 80to 85 degrees Fahrenheit, 85 to 90 degrees Fahrenheit, 90 to 95 degreesFahrenheit, 95 to 100 degrees Fahrenheit, 100 to 110 degrees Fahrenheit,110 to 120 degrees Fahrenheit, 120 to 130 degrees Fahrenheit, 130 to 140degrees Fahrenheit, 140 to 150 degrees Fahrenheit, 150 to 160 degreesFahrenheit, or 160 to 175 degrees Fahrenheit.

In embodiments, the cannabis is heated to a temperature ranging from 50to 60 degrees Fahrenheit, 60 to 65 degrees Fahrenheit, 65 to 70 degreesFahrenheit, 70 to 75 degrees Fahrenheit, 75 to 80 degrees Fahrenheit, 80to 85 degrees Fahrenheit, 85 to 90 degrees Fahrenheit, 90 to 95 degreesFahrenheit, 95 to 100 degrees Fahrenheit, 100 to 110 degrees Fahrenheit,110 to 120 degrees Fahrenheit, 120 to 130 degrees Fahrenheit, 130 to 140degrees Fahrenheit, 140 to 150 degrees Fahrenheit, 150 to 160 degreesFahrenheit, or 160 to 175 degrees Fahrenheit.

In embodiments, a vacuum (VAC*) is pulled on cannabis (107*, 207*) whilethe heater (HTR1*) is heating the cannabis (107*, 207*) to aide incarbon dioxide removal. In embodiments, a vacuum (VAC*) is pulled on thecannabis (107*, 207*) while the heater (HTR1*) is heating the cannabis(107*, 207*) to a pressure that ranges from 0.5 inches of water to 30inches of water. In embodiments, a vacuum (VAC*) is pulled on thecannabis (107*, 207*) while the heater (HTR1*) is heating the cannabis(107*, 207*) to a pressure that ranges from 5 inches of water to 90inches of water. In embodiments, a vacuum (VAC*) is pulled on thecannabis (107*, 207*) while the heater (HTR1*) is heating the cannabis(107*, 207*) to a pressure that ranges from 2 pounds per square inchabsolute to 14.69 pounds per square inch absolute. In embodiments, thecannabis (107*, 207*) is heated by the heater (HTR1*) for a duration of45 minutes to 2 hours. In embodiments, the cannabis (107*, 207*) isheated by the heater (HTR1*) for a duration of 1 hour to 3 hours. Inembodiments, the cannabis (107*, 207*) is heated by the heater (HTR1*)for a duration of 2 hour to 24 hours.

FIG. 17A′

FIG. 17A′ shows one non-limiting embodiment of a volatiles extractionsystem (VES*) that is configured to extract volatiles from cannabis(107*, 207*) with a first solvent (SOLV1*). The volatiles extractionsystem (VES*) is configured to separate volatiles (VOLT*) from cannabis(107*, 207*). The volatiles extraction system (VES*) is configured toaccept cannabis (107*, 207*), or heated cannabis (HT1*), ground cannabis(GR1*), trimmed cannabis (TR1*), and/or combinations thereof. Inembodiments, the cannabis (107*, 207*), heated cannabis (HT1*), groundcannabis (GR1*), and/or trimmed cannabis (TR1*) may be weighed with amass sensor (MS-VES*) prior to being introduced to the volatilesextraction system (VES*). The volatiles extraction system (VES*) isconfigured to accept insects and separate lipids therefrom.

The volatiles (VOLT*) include one or more from the group consisting ofoil, wax, terpenes. The volatiles (VOLT*) include cannabinoids. Inembodiments, the terpenes include one or more from the group consistingof limonene, humulene, pinene, linalool, caryophyllene, myrcene,eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the terpenes include one or more from the groupconsisting of alpha bisabolol, alpha pinene, beta caryophyllene, betapinene, borneol, camphene, caryophyllene oxide, cineole, delta 3 carene,eucalyptol, fenchol, fenchone, geraniol, guaiol, humulene, isopulegol,limonene, linalool, myrcene, nerol, nerolidol, ocimene, phytol,pulegone, terpinene, terpineol, terpinolene, valencene, and combinationsthereof.

In embodiments, the terpenes may be extracted from the volatiles. Inembodiments, the terpenes may be extracted from the volatiles and thenmixed with the concentrated volatiles. In embodiments, the terpenes maybe extracted from the volatiles and then mixed with the concentratedvolatiles after wax and solvent are removed from the volatiles. Inembodiments, the terpenes mixed with the concentrated volatiles are notfrom a cannabis plant. In embodiments, the terpenes mixed with theconcentrated volatiles are from a cannabis plant. In embodiments, theterpenes are produced by chemical synthesis from petrochemicals,hydrocarbons, plants, conifer trees, or insects. In embodiments, theterpenes include isoprenoids.

In embodiments, the terpenes include at least one organic carboncontaining chemical compound. In embodiments, the terpenes include oneor more from the group consisting of limonene, humulene, pinene,linalool, caryophyllene, myrcene, eucalyptol, nerolidol, bisablol, andphytol. In embodiments, limonene includes1-Methyl-4-(1-methylethenyl)-cyclohexene. In embodiments, humuleneincludes 2,6,6,9-Tetramethyl-1,4-8-cycloundecatriene. In embodiments,pinene includes (1S,5S)-2,6,6-trimethylbicyclo[3.1.1]hept-2-ene. Inembodiments, linalool includes 3,7-Dimethylocta-1,6-dien-3-ol. Inembodiments, caryophyllene includes(1R,4E,9S)-4,11,11-Trimethyl-8-methylidenebicyclo[7.2.0]undec-4-ene. Inembodiments, myrcene includes 7-Methyl-3-methylene-1,6-octadiene. Inembodiments, eucalyptol includes1,3,3-Trimethyl-2-oxabicyclo[2,2,2]octane. In embodiments, nerolidolincludes 3,7,11-Trimethyl-1,6,10-dodecatrien-3-ol. In embodiments,bisablol includes 6-methyl-2-(4-methylcyclohex-3-en-1-yl)hept-5-en-2-ol.In embodiments, phytol includes(2E,7R,11R)-3,7,11,15-tetramethyl-2-hexadecen-1-ol.

The volatiles extraction system (VES*) extracts volatiles (VOLT*) fromcannabis with use of a first solvent (SOLV1*). In embodiments, the firstsolvent (SOLV1*) includes one or more from the group consisting ofacetone, alcohol, oil, butane, butter, carbon dioxide, coconut oil,ethanol, gas, gaseous carbon dioxide, hexane, insect lipids, isobutane,isopropanol, liquid carbon dioxide, liquid, naphtha, olive oil, pentane,propane, R134 refrigerant gas, subcritical carbon dioxide, supercriticalcarbon dioxide, and vapor. In embodiments, the first solvent (SOLV1*)includes one or more from the group consisting of petroleum ether,pentane, n-hexane, hexanes, diethyl ether, ethyl acetate, and ethanol.

The volatiles extraction system (VES*) has an interior (VESI*) that isconfigured to mix cannabis (107*, 207*), heated cannabis (HT1*), groundcannabis (GR1*), and/or trimmed cannabis (TR1*) with a first solvent(SOLV1*). The volatiles extraction system (VES*) is configured to accepta first solvent (SOLV1*). The first solvent (SOLV1*) is configured tocontact the cannabis (107*, 207*), heated cannabis (HT1*), groundcannabis (GR1*), and/or trimmed cannabis (TR1*) within the interior(VESI*) of the volatiles extraction system (VES*).

An output of the volatiles extraction system (VES*) is a first solventand volatiles mixture (FSVM*). The first solvent and volatiles mixture(FSVM*) is at least a mixture of volatiles (VOLT*) and the first solvent(SOLV1*). In embodiments, the first solvent and volatiles mixture(FSVM*) is a mixture of oil, wax, terpenes and first solvent (SOLV1*).In embodiments, the oil contains cannabinoids. In embodiments, the firstsolvent and volatiles mixture (FSVM*) is a mixture of oil, wax, andfirst solvent (SOLV1*). In embodiments, the first solvent and volatilesmixture (FSVM*) is a mixture of oil and first solvent (SOLV1*). Thefirst solvent and volatiles mixture (FSVM*) is transferred from thevolatiles extraction system (VES*) to the first solvent separationsystem (SSS*).

The first solvent separation system (SSS*) is configured to separate thevolatiles (VOLT*) from the first solvent and volatiles mixture (FSVM*).The first solvent separation system (SSS*) has an interior (SSSI*). Thefirst solvent and volatiles mixture (FSVM*) is transferred from theinterior (VESI*) of the volatiles extraction system (VES*) to theinterior (SSSI*) of the first solvent separation system (SSS*).

In embodiments, the interior (VESI*) of the volatiles extraction system(VES*) is in thermal contact with a first volatiles extraction heatexchanger (VS-HX1*). The first volatiles extraction heat exchanger(VS-HX1*) is configured to add and/or remove heat from the interior(VESI*) of the volatiles extraction system (VES*). The first volatilesextraction heat exchanger (VS-HX1*) is configured to add and/or removeheat from the cannabis within the interior (VESI*) of the volatilesextraction system (VES*). the first volatiles extraction heat exchanger(VS-HX1*) is configured to remove heat from the first solvent andvolatiles mixture (FSVM*) within the interior (VESI*) of the volatilesextraction system (VES*). In embodiments, the interior (SSSI*) of thefirst solvent separation system (SSS*) is in thermal contact with asecond volatiles extraction heat exchanger (VS-HX2*). The secondvolatiles extraction heat exchanger (VS-HX2) is configured to add and/orremove heat from the interior (SSSI*) of the first solvent separationsystem (SSS*).

The first volatiles extraction heat exchanger (VS-HX1*) includes a firstheat transfer medium (VF1C*). The second volatiles extraction heatexchanger (VS-HX2*) includes a second heat transfer medium (VF2C*). Inembodiments, the second coolant (VF2C*) configured to add and/or removeheat from the interior (SSSI*) of the first solvent separation system(SSS*) is the first heat transfer medium (VF1C) that was used to addand/or remove heat from the interior (VESI*) of the volatiles extractionsystem (VES*). In embodiments, the first heat transfer medium (VF1C*)configured to add and/or remove heat from the interior (VESI*) of thevolatiles extraction system (VES*) is the second heat transfer medium(VF2C) used to add and/or remove heat from the interior (SSSI*) of thefirst solvent separation system (SSS*). In embodiments, the first heattransfer medium (VF1C*) and/or the second heat transfer medium (VF2C*)include a heated or cooled liquid. In embodiments, the first heattransfer medium (VF1C*) and/or the second heat transfer medium (VF2C*)include a refrigerated liquid, including water, an alcohol, ethyleneglycol, ethylene alcohol, an oil, and an organic compound.

In embodiments, the first heat transfer medium (VF1C*) maintains theinterior (VESI*) of the volatiles extraction system (VES*) at atemperature range including one or more ranges selected from the groupconsisting of: between about 32 degrees Fahrenheit to about 40 degreesFahrenheit; between about 40 degrees Fahrenheit to about 45 degreesFahrenheit; between about 45 degrees Fahrenheit to about 50 degreesFahrenheit; between about 50 degrees Fahrenheit to about 55 degreesFahrenheit; between about 55 degrees Fahrenheit to about 60 degreesFahrenheit; between about 60 degrees Fahrenheit to about 65 degreesFahrenheit; between about 65 degrees Fahrenheit to about 70 degreesFahrenheit; between about 70 degrees Fahrenheit to about 75 degreesFahrenheit; between about 75 degrees Fahrenheit to about 80 degreesFahrenheit; between about 80 degrees Fahrenheit to about 85 degreesFahrenheit; between about 85 degrees Fahrenheit to about 90 degreesFahrenheit; between about 90 degrees Fahrenheit to about 95 degreesFahrenheit; between about 95 degrees Fahrenheit to about 100 degreesFahrenheit; between about 100 degrees Fahrenheit to about 105 degreesFahrenheit; between about 105 degrees Fahrenheit to about 110 degreesFahrenheit; between about 110 degrees Fahrenheit to about 115 degreesFahrenheit; between about 115 degrees Fahrenheit to about 120 degreesFahrenheit; between about 120 degrees Fahrenheit to about 130 degreesFahrenheit; between about 130 degrees Fahrenheit to about 160 degreesFahrenheit; between about 160 degrees Fahrenheit to about 190 degreesFahrenheit.

In embodiments, the second heat transfer medium(VF2C*) maintainsinterior (SSSI*) of the first solvent separation system (SSS*) at atemperature range including one or more ranges selected from the groupconsisting of: between about 32 degrees Fahrenheit to about 40 degreesFahrenheit; between about 40 degrees Fahrenheit to about 45 degreesFahrenheit; between about 45 degrees Fahrenheit to about 50 degreesFahrenheit; between about 50 degrees Fahrenheit to about 55 degreesFahrenheit; between about 55 degrees Fahrenheit to about 60 degreesFahrenheit; between about 60 degrees Fahrenheit to about 65 degreesFahrenheit; between about 65 degrees Fahrenheit to about 70 degreesFahrenheit; between about 70 degrees Fahrenheit to about 75 degreesFahrenheit; between about 75 degrees Fahrenheit to about 80 degreesFahrenheit; between about 80 degrees Fahrenheit to about 85 degreesFahrenheit; between about 85 degrees Fahrenheit to about 90 degreesFahrenheit; between about 90 degrees Fahrenheit to about 95 degreesFahrenheit; between about 95 degrees Fahrenheit to about 100 degreesFahrenheit; between about 100 degrees Fahrenheit to about 105 degreesFahrenheit; between about 105 degrees Fahrenheit to about 110 degreesFahrenheit; between about 110 degrees Fahrenheit to about 115 degreesFahrenheit; between about 115 degrees Fahrenheit to about 120 degreesFahrenheit; between about 120 degrees Fahrenheit to about 130 degreesFahrenheit; between about 130 degrees Fahrenheit to about 160 degreesFahrenheit; between about 160 degrees Fahrenheit to about 190 degreesFahrenheit.

In embodiments, the pressure within the interior (VESI*) of thevolatiles extraction system (VES*) is greater than the pressure withinthe interior (SSSI*) of the first solvent separation system (SSS*). Inembodiments, the pressure within the interior (VESI*) of the volatilesextraction system (VES*) is less than the pressure within the interior(SSSI*) of the first solvent separation system (SSS*). In embodiments,the pressure within the interior (VESI*) of the volatiles extractionsystem (VES*) is equal to the pressure within the interior (SSSI*) ofthe first solvent separation system (SSS*).

The first solvent separation system (SSS*) outputs a volatiles (VOLT*)and a separated first solvent (SOLV1-S*). The volatiles (VOLT*) may bethen mixed with a second solvent (SOLV2*) as described in FIG. 17C′. Thevolatiles (VOLT*) may alternately by mixed with insects which includeone or more from the group consisting of Orthoptera order of insects,grasshoppers, crickets, cave crickets, Jerusalem crickets, katydids,weta, lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,worms, bees, centipedes, cockroaches, dragonflies, beetles, scorpions,tarantulas, termites, insect lipids, and insect oil.

The volatiles (VOLT*) may alternately by mixed with insects whichinclude one or more from the group consisting of Anthocoridae, minutepirate bugs, pirate bugs, flower bugs, the genus Orius, omnivorous bugs,carnivorous bugs, Orthoptera order of insects, grasshoppers, crickets,katydids, weta, lubber, acrida, locusts, mites, spider mites, predatorymites, Neoseiulus Fallacis, genus of mites that are in the Phytoseiidaefamily, arthropods, hexapods, beetles, cicadas, beetles, nematodes,mealworms, bats, mammals of the order Chiroptera, yellow mealwormbeetles, Tenebrio Molitor, Tetranychus Urticae, carnivorous arthropods,omnivorous arthropods, green lacewings, insects in the familyChrysopidae, insects in the order Neuroptera, mantidflies, black soldierflies, larvae, fly larvae, insect larvae, arthropod larvae, blacksoldier fly larvae, Hermetia illucens, antlions, mosquitos, Coloradopotato beetle, Leptinotarsa decemlineata, Encarsia Formosa, whiteflyparasites, ladybugs, spiders, dragonflies, orb-weaving spiders,arachnids, members of the spider family Araneidae, praying mantis,arachnids, eight-legged arthropods, six-legged arthropods, fallarmyworm, Spodoptera frugiperda, species in the order Lepidoptera,diamondback moths, cabbage moths, moth species of the family Plutellidaeand genus Plutella, moth species of the family Plutellidae, drosophilasuzukii, spotted wing drosophila, Ceratitis capitata, Mediterraneanfruit flies, medfly. The volatiles extraction system (VES*) isconfigured to operate in a plurality of modes of operation. In a firstmode of operation, the volatiles extraction system (VES*) separatesterpenes from the cannabis. The first mode of operation may take placeat a first temperature and a first pressure. In a second mode ofoperation, the volatiles extraction system (VES*) separates othervolatiles (VOLT*) from the cannabis. The second mode of operation maytake place at a second temperature and a first pressure. In embodiments,the second temperature is greater than the first temperature. Inembodiments, the second pressure is greater than the first pressure.

In embodiments, the interior (VESI*) of the volatiles extraction system(VES*) is configured to operate at a pressure range including one ormore ranges selected from the group consisting of: 500 PSI to 1,000 PSI,1,000 PSI to 1,500 PSI, 1,500 PSI to 2,000 PSI, 2,000 PSI to 2,500 PSI,2,500 PSI to 3,000 PSI, 3,500 PSI to 4,000 PSI, 4,000 PSI to 4,500 PSI,4,500 PSI to 5,000 PSI, and 5,000 PSI to 6,000 PSI.

In embodiments, the interior (SSSI*) of the first solvent separationsystem (SSS*) is configured to operate at a pressure range including oneor more ranges selected from the group consisting of: 500 PSI to 1,000PSI, 1,000 PSI to 1,500 PSI, 1,500 PSI to 2,000 PSI, 2,000 PSI to 2,500PSI, 2,500 PSI to 3,000 PSI, 3,500 PSI to 4,000 PSI, 4,000 PSI to 4,500PSI, 4,500 PSI to 5,000 PSI, and 5,000 PSI to 6,000 PSI.

In embodiments, the difference in pressure between the interior (VESI*)of the volatiles extraction system (VES*) and the interior (SSSI*) ofthe first solvent separation system (SSS*) including one or more rangesselected from the group consisting of: 100 PSI to 150 PSI, 150 PSI to250 PSI, 250 PSI to 350 PSI, 350 PSI to 500 PSI, 500 PSI to 1,000 PSI,1,000 PSI to 1,500 PSI, 1,500 PSI to 2,000 PSI, 2,000 PSI to 2,500 PSI,2,500 PSI to 3,000 PSI, 3,500 PSI to 4,000 PSI, 4,000 PSI to 4,500 PSI,4,500 PSI to 5,000 PSI, and 5,000 PSI to 6,000 PSI.

In embodiments, cannabinoids may extracted from the cannabis withethanol for a time duration ranging from 1 minute to 2 minutes, 2minutes to 4 minutes, 4 minutes to 6 minutes, 6 minutes to 8 minutes, 8minutes to 10 minutes, 10 minutes to 12 minutes, 12 minutes to 14minutes, 14 minutes to 16 minutes, 16 minutes to 18 minutes, 18 minutesto 20 minutes, 20 minutes to 25 minutes, 25 minutes to 30 minutes, 30minutes to 35 minutes, 35 minutes to 40 minutes, 40 minutes to 45minutes, 45 minutes to 50 minutes, 50 minutes to 55 minutes, 55 minutesto 1 hour, 1 hour to 1.5 hours, 1.5 hours to 2 hours, 2 hours to 2.5hours, 2.5 hours to 3 hours, 3 hours to 3.5 hours, 3.5 hours to 4 hours,4 hours to 4.5 hours, 4.5 hours to 5 hours, 5 hours to 5.5 hours, 5.5hours to 6 hours, 6 hours to 18 hours, 18 hours to 24 hours, 24 hours to36 hours, 36 hours to 48 hours, 48 hours to 60 hours, 60 hours to 72hours, 72 hours to 84 hours, or 84 hours to 96 hours.

In embodiments, cannabinoids may extracted from the cannabis with thefirst solvent for a time duration ranging from 1 second to 15 seconds,15 seconds to 30 seconds, 30 seconds to 1 minute, 1 minute to 2 minutes,2 minutes to 4 minutes, 4 minutes to 6 minutes, 6 minutes to 8 minutes,8 minutes to 10 minutes, 10 minutes to 12 minutes, 12 minutes to 14minutes, 14 minutes to 16 minutes, 16 minutes to 18 minutes, 18 minutesto 20 minutes, 20 minutes to 25 minutes, 25 minutes to 30 minutes, 30minutes to 35 minutes, 35 minutes to 40 minutes, 40 minutes to 45minutes, 45 minutes to 50 minutes, 50 minutes to 55 minutes, 55 minutesto 1 hour, 1 hour to 1.5 hours, 1.5 hours to 2 hours, 2 hours to 2.5hours, 2.5 hours to 3 hours, 3 hours to 3.5 hours, 3.5 hours to 4 hours,4 hours to 4.5 hours, 4.5 hours to 5 hours, 5 hours to 5.5 hours, 5.5hours to 6 hours, 6 hours to 18 hours, 18 hours to 24 hours, 24 hours to36 hours, 36 hours to 48 hours, 48 hours to 60 hours, 60 hours to 72hours, 72 hours to 84 hours, or 84 hours to 96 hours.

FIG. 17A″

FIG. 17A″ shows one non-limiting embodiment of a volatiles extractionsystem (VES*) that is configured to extract volatiles from cannabis(107*, 207*) with a chilled ethanol separation system (CESS).

In embodiments, the volatiles extraction system (VES*) is configured toseparate volatiles (VOLT*) from cannabis (107*, 207*) the cannabisincludes plant matter, leaves, stems, and/or buds. The volatilesextraction system (VES*) is configured to accept cannabis (107*, 207*),or heated cannabis (HT1*), ground cannabis (GR1*), trimmed cannabis(TR1*), cannabis trimmings (TR2*), and optionally including a cannabisand insects mixture and/or combinations thereof. In embodiments, thecannabis (107*, 207*), or heated cannabis (HT1*), ground cannabis(GR1*), trimmed cannabis (TR1*), cannabis trimmings (TR2*), andoptionally including a cannabis and insects mixture may be weighed witha mass sensor (MS-VES*) prior to being introduced to the volatilesextraction system (VES*).

The volatiles (VOLT*) include one or more from the group consisting ofoil, wax, terpenes. The volatiles (VOLT*) include cannabinoids. Inembodiments, the terpenes may be extracted from the volatiles. Inembodiments, the terpenes may be extracted from the volatiles and thenmixed with the concentrated volatiles. In embodiments, the terpenes maybe extracted from the volatiles and then mixed with the concentratedvolatiles after wax and solvent are removed from the volatiles. Inembodiments, the terpenes mixed with the concentrated volatiles are notfrom a cannabis plant. In embodiments, the terpenes mixed with theconcentrated volatiles are from a cannabis plant.

The volatiles extraction system (VES*) extracts volatiles (VOLT*) fromcannabis with use of a first solvent (SOLV1*). In embodiments, The firstsolvent (SOLV1*) includes chilled ethanol. In embodiments, the firstsolvent (SOLV1*) includes a chilled ethanol and water mixture. Inembodiments, the water within the chilled ethanol and water mixtureincludes treated water, the treated water may be distilled, membranetreated water, adsorbent treated water, cation and/or anion treatedwater, or any types of treated water mentioned in this specification.

The volatiles extraction system (VES*) has an interior (VESI*) that isconfigured to mix cannabis (107*, 207*), or heated cannabis (HT1*),ground cannabis (GR1*), trimmed cannabis (TR1*), cannabis trimmings(TR2*), and optionally including a cannabis and insects mixture thefirst solvent (SOLV1*). The volatiles extraction system (VES*) isconfigured to accept a first solvent (SOLV1*). The first solvent(SOLV1*) is configured to contact the cannabis (107*, 207*), or heatedcannabis (HT1*), ground cannabis (GR1*), trimmed cannabis (TR1*),cannabis trimmings (TR2*), and optionally including a cannabis andinsects mixture within the interior (VESI*) of the volatiles extractionsystem (VES*).

In embodiments, the volatiles extraction system (VES*) outputs a mixtureof cannabinoids and ethanol as a first solvent and volatiles mixture(FSVM*). The first solvent and volatiles mixture (FSVM*) is at least amixture of volatiles (VOLT*) and the first solvent (SOLV1*). Inembodiments, the first solvent and volatiles mixture (FSVM*) is amixture of oil, wax, terpenes and first solvent (SOLV1*). Inembodiments, the oil contains cannabinoids. In embodiments, the firstsolvent and volatiles mixture (FSVM*) is a mixture of oil, wax, andfirst solvent (SOLV1*). In embodiments, the first solvent and volatilesmixture (FSVM*) is a mixture of oil and first solvent (SOLV1*). Thefirst solvent and volatiles mixture (FSVM*) is transferred from thevolatiles extraction system (VES*) to the first solids separation system(SSS**). In embodiments, a first solids separation system (SSS**) and asecond solids separation system (SSS***) may be used to remove the firstsolvent and volatiles mixture (FSVM*) from the volatiles extractionsystem (VES*).

The first solids separation system (SSS**) is configured to separate theplant matter (leaves, stems, and/or buds) from the first solvent andvolatiles mixture (FSVM*). The first solids separation system (SSS**)has an interior (SSSI*). The first solvent and volatiles mixture (FSVM*)is transferred from the interior (VESI*) of the volatiles extractionsystem (VES*) to the interior (SSSI*) of the first solids separationsystem (SSS**).

In embodiments, the interior (VESI*) of the volatiles extraction system(VES*) is in thermal contact with a first volatiles extraction heatexchanger (VS-HX1*). The first volatiles extraction heat exchanger(VS-HX1*) is configured to add and/or remove heat from the interior(VESI*) of the volatiles extraction system (VES*). The first volatilesextraction heat exchanger (VS-HX1*) is configured to add and/or removeheat from the cannabis within the interior (VESI*) of the volatilesextraction system (VES*). the first volatiles extraction heat exchanger(VS-HX1*) is configured to remove heat from the first solvent andvolatiles mixture (FSVM*) within the interior (VESI*) of the volatilesextraction system (VES*). In embodiments, the interior (SSSI*) of thefirst solids separation system (SSS**) is in thermal contact with asecond volatiles extraction heat exchanger (VS-HX2*). The secondvolatiles extraction heat exchanger (VS-HX2) is configured to add and/orremove heat from the interior (SSSI*) of the first solids separationsystem (SSS**).

The first volatiles extraction heat exchanger (VS-HX1*) includes a firstheat transfer medium (VF1C*). The second volatiles extraction heatexchanger (VS-HX2*) includes a second heat transfer medium (VF2C*). Inembodiments, the second coolant (VF2C*) configured to add and/or removeheat from the interior (SSSI*) of the first solids separation system(SSS**) is the first heat transfer medium (VF1C) that was used to addand/or remove heat from the interior (VESI*) of the volatiles extractionsystem (VES*). In embodiments, the first heat transfer medium (VF1C*)configured to add and/or remove heat from the interior (VESI*) of thevolatiles extraction system (VES*) is the second heat transfer medium(VF2C) used to add and/or remove heat from the interior (SSSI*) of thefirst solids separation system (SSS**). In embodiments, the first heattransfer medium (VF1C*) and/or the second heat transfer medium (VF2C*)include a heated or cooled liquid. In embodiments, the first heattransfer medium (VF1C*) and/or the second heat transfer medium (VF2C*)include a refrigerated liquid, including water, an alcohol, ethyleneglycol, ethylene alcohol, an oil, liquid carbon dioxide, a refrigerant,and an organic compound.

In embodiments, the first heat transfer medium (VF1C*) maintains theinterior (VESI*) of the volatiles extraction system (VES*) at atemperature range including one or more ranges selected from the groupconsisting of: between about 32 degrees Fahrenheit to about 40 degreesFahrenheit; between about 40 degrees Fahrenheit to about 45 degreesFahrenheit; between about 45 degrees Fahrenheit to about 50 degreesFahrenheit; between about 50 degrees Fahrenheit to about 55 degreesFahrenheit; between about 55 degrees Fahrenheit to about 60 degreesFahrenheit; between about 60 degrees Fahrenheit to about 65 degreesFahrenheit; between about 65 degrees Fahrenheit to about 70 degreesFahrenheit; between about 70 degrees Fahrenheit to about 75 degreesFahrenheit; between about 75 degrees Fahrenheit to about 80 degreesFahrenheit; between about 80 degrees Fahrenheit to about 85 degreesFahrenheit; between about 85 degrees Fahrenheit to about 90 degreesFahrenheit; between about 90 degrees Fahrenheit to about 95 degreesFahrenheit; between about 95 degrees Fahrenheit to about 100 degreesFahrenheit; between about 100 degrees Fahrenheit to about 105 degreesFahrenheit; between about 105 degrees Fahrenheit to about 110 degreesFahrenheit; between about 110 degrees Fahrenheit to about 115 degreesFahrenheit; between about 115 degrees Fahrenheit to about 120 degreesFahrenheit; between about 120 degrees Fahrenheit to about 130 degreesFahrenheit; between about 130 degrees Fahrenheit to about 160 degreesFahrenheit; between about 160 degrees Fahrenheit to about 190 degreesFahrenheit.

In embodiments, the first heat transfer medium (VF1C*) maintains theinterior (VESI*) of the volatiles extraction system (VES*) at atemperature range including one or more ranges selected from the groupconsisting of: 32 degrees Fahrenheit to 0 degrees Fahrenheit, 0 degreesFahrenheit to −10 degrees Fahrenheit, −10 degrees Fahrenheit to −20degrees Fahrenheit, −20 degrees Fahrenheit to −30 degrees Fahrenheit,−30 degrees Fahrenheit to −40 degrees Fahrenheit, −40 degrees Fahrenheitto −50 degrees Fahrenheit, −50 degrees Fahrenheit to −75 degreesFahrenheit, −75 degrees Fahrenheit to −100 degrees Fahrenheit, −100degrees Fahrenheit to −125 degrees Fahrenheit, or −135 degreesFahrenheit to −150 degrees Fahrenheit.

In embodiments, the second heat transfer medium(VF2C*) maintainsinterior (SSSI*) of the first solids separation system (SSS**) at atemperature range including one or more ranges selected from the groupconsisting of: between about 32 degrees Fahrenheit to about 40 degreesFahrenheit; between about 40 degrees Fahrenheit to about 45 degreesFahrenheit; between about 45 degrees Fahrenheit to about 50 degreesFahrenheit; between about 50 degrees Fahrenheit to about 55 degreesFahrenheit; between about 55 degrees Fahrenheit to about 60 degreesFahrenheit; between about 60 degrees Fahrenheit to about 65 degreesFahrenheit; between about 65 degrees Fahrenheit to about 70 degreesFahrenheit; between about 70 degrees Fahrenheit to about 75 degreesFahrenheit; between about 75 degrees Fahrenheit to about 80 degreesFahrenheit; between about 80 degrees Fahrenheit to about 85 degreesFahrenheit; between about 85 degrees Fahrenheit to about 90 degreesFahrenheit; between about 90 degrees Fahrenheit to about 95 degreesFahrenheit; between about 95 degrees Fahrenheit to about 100 degreesFahrenheit; between about 100 degrees Fahrenheit to about 105 degreesFahrenheit; between about 105 degrees Fahrenheit to about 110 degreesFahrenheit; between about 110 degrees Fahrenheit to about 115 degreesFahrenheit; between about 115 degrees Fahrenheit to about 120 degreesFahrenheit; between about 120 degrees Fahrenheit to about 130 degreesFahrenheit; between about 130 degrees Fahrenheit to about 160 degreesFahrenheit; between about 160 degrees Fahrenheit to about 190 degreesFahrenheit.

In embodiments, the second heat transfer medium(VF2C*) maintainsinterior (SSSI*) of the first solids separation system (SSS**) at atemperature range including one or more ranges selected from the groupconsisting of: 32 degrees Fahrenheit to 0 degrees Fahrenheit, 0 degreesFahrenheit to −10 degrees Fahrenheit, −10 degrees Fahrenheit to −20degrees Fahrenheit, −20 degrees Fahrenheit to −30 degrees Fahrenheit,−30 degrees Fahrenheit to −40 degrees Fahrenheit, −40 degrees Fahrenheitto −50 degrees Fahrenheit, −50 degrees Fahrenheit to −75 degreesFahrenheit, −75 degrees Fahrenheit to −100 degrees Fahrenheit, −100degrees Fahrenheit to −125 degrees Fahrenheit, or −135 degreesFahrenheit to −150 degrees Fahrenheit.

In embodiments, the pressure within the interior (VESI*) of thevolatiles extraction system (VES*) is greater than the pressure withinthe interior (SSSI*) of the first solids separation system (SSS**). Inembodiments, the pressure within the interior (VESI*) of the volatilesextraction system (VES*) is less than the pressure within the interior(SSSI*) of the first solids separation system (SSS**). In embodiments,the pressure within the interior (VESI*) of the volatiles extractionsystem (VES*) is equal to the pressure within the interior (SSSI*) ofthe first solids separation system (SSS**).

The first solids separation system (SSS**) outputs a volatiles andethanol mixture (VOLT**) and a separated solids (SOLIDSV), the solids(SOLIDSV) include plant matter. The volatiles and ethanol mixture(VOLT**) includes volatiles (VOLT*) and ethanol (SOLVETH). Inembodiments, the ethanol (SOLVETH) includes a water and ethanol mixture.In embodiments, the water includes treated water.

The volatiles (VOLT*) may be then transferred to the solvent cooler(SOLV-C*) as shown on FIG. 17C′. The volatiles and ethanol mixture(VOLT**) may be cooled together with carbon dioxide extracted cannabisoil.

In embodiments, cannabinoids may extracted from the cannabis with thefirst solvent within the volatiles extraction system (VES*) for a timeduration ranging from 1 second to 15 seconds, 15 seconds to 30 seconds,30 seconds to 1 minute, 1 minute to 2 minutes, 2 minutes to 4 minutes, 4minutes to 6 minutes, 6 minutes to 8 minutes, 8 minutes to 10 minutes,10 minutes to 12 minutes, 12 minutes to 14 minutes, 14 minutes to 16minutes, 16 minutes to 18 minutes, 18 minutes to 20 minutes, 20 minutesto 25 minutes, 25 minutes to 30 minutes, 30 minutes to 35 minutes, 35minutes to 40 minutes, 40 minutes to 45 minutes, 45 minutes to 50minutes, 50 minutes to 55 minutes, 55 minutes to 1 hour, 1 hour to 1.5hours, 1.5 hours to 2 hours, 2 hours to 2.5 hours, 2.5 hours to 3 hours,3 hours to 3.5 hours, 3.5 hours to 4 hours, 4 hours to 4.5 hours, 4.5hours to 5 hours, 5 hours to 5.5 hours, 5.5 hours to 6 hours. Preferablythe shorter the duration of ethanol extraction is preferred so as toonly separate volatiles from the cannabis and not other undesirablecompounds such as chlorophyll and/or wax.

FIG. 17B′

FIG. 17B′ shows a plurality of volatiles extraction systems (VES1*,VES2*) equipped with one first solvent separation system (SSS*). Thefirst volatiles extraction system (VES1*) has an interior (VES1I*) thatis configured to mix cannabis (107*, 207*), heated cannabis (HT1*),ground cannabis (GR1*), or trimmed cannabis (TR1*) with a first solvent(SOLV1*). The second volatiles extraction system (VES2*) has an interior(VES1I*) that is configured to mix cannabis (107*, 207*), heatedcannabis (HT1*), ground cannabis (GR1*), or trimmed cannabis (TR1*) witha first solvent (SOLV1*).

FIG. 17B′ shows a first cannabis portion (FCS*) introduced to the firstvolatiles extraction system (VES1*) and a second cannabis portion (SCS*)introduced to the second volatiles extraction system (VES2*). The firstcannabis portion (FCS*) may be weighed prior to being introduced to thefirst volatiles extraction system (VES1*). The second cannabis portion(SCS*) may be weighed prior to being introduced to the second volatilesextraction system (VES2*). The first cannabis portion (FCS*) and/or thesecond cannabis portion (SCS*) may be either cannabis (107*, 207*), orheated cannabis (HT1*), ground cannabis (GR1*), trimmed cannabis (TR1*),or combinations thereof.

A primary first solvent and volatiles mixture (FSVMA*) is dischargedfrom the first volatiles extraction system (VES1*). A secondary firstsolvent and volatiles mixture (FSVMB*) is discharged from the secondvolatiles extraction system (VES1*). The primary first solvent andvolatiles mixture (FSVMA*) and secondary first solvent and volatilesmixture (FSVMB*) are combined and introduced to the first solventseparation system (SSS*).

FIG. 17C′

FIG. 17C′ shows a volatiles and solvent mixing system (VSMS*) that isconfigured to mix the volatiles (VOLT*) with a second solvent (SOLV2*).The volatiles (VOLT*) that are introduced to the interior (VSMSI*) ofthe volatiles and solvent mixing system (VSMS*) are transferred from thevolatiles extraction systems (VES*, VES1*, VES2*) via the first solventseparation system (SSS*) as shown in FIGS. 17A′ and 17B′.

In embodiments, the second solvent (SOLV2*) includes one or more fromthe group consisting of a liquid, acetone, alcohol, oil, ethanol. Inembodiments, the second solvent (SOLV2*) includes one or more from thegroup consisting of petroleum ether, pentane, n-hexane, hexanes, diethylether, ethyl acetate, and ethanol. The second solvent (SOLV2*) can beweighed with a mass sensor (MS-SOLV2*) prior to being introduced to theinterior (VSMSI*) of the volatiles and solvent mixing system (VSMS*).The volatiles (VOLT*) may also be weighed with a mass sensor (MS-VOLT*)prior to being introduced to the interior (VSMSI*) of the volatiles andsolvent mixing system (VSMS*). The second solvent (SOLV2*) and volatiles(VOLT*) are mixed within the interior (VSMSI*) of the volatiles andsolvent mixing system (VSMS*).

The volatiles (VOLT*) and second solvent (SOLV2*) may be are mixed atvarying mass ratios. The volatiles (VOLT*) to second solvent (SOLV2*)mixing mass ratio is the pounds of volatiles (VOLT*) per pounds ofsecond solvent (SOLV2*). In embodiments, the mixing mass ratio ofvolatiles (VOLT*) to the second solvent (SOLV2*) ranges from 1 pound ofvolatiles (VOLT*) per 1 pound of second solvent (SOLV2*), so this wouldbe a mixing mass ratio of 1/1 or 1; In embodiments, the mixing massratio of volatiles (VOLT*) to the second solvent (SOLV2*) ranges from 1pound of volatiles (VOLT*) per 2 pounds of second solvent (SOLV2*), sothis would be a mixing mass ratio of 1/2 or 0.5; In embodiments, themixing mass ratio of volatiles (VOLT*) to the second solvent (SOLV2*)ranges from 1 pound of volatiles (VOLT*) per 3 pounds of second solvent(SOLV2*), so this would be a mixing mass ratio of 1/3 or 0.33; Inembodiments, the mixing mass ratio of volatiles (VOLT*) to the secondsolvent (SOLV2*) ranges from 1 pound of volatiles (VOLT*) per 4 poundsof second solvent (SOLV2*), so this would be a mixing mass ratio of 1/4or 0.25; In embodiments, the mixing mass ratio of volatiles (VOLT*) tothe second solvent (SOLV2*) ranges from 1 pound of volatiles (VOLT*) per5 pounds of second solvent (SOLV2*), so this would be a mixing massratio of 1/5 or 0.2; In embodiments, the mixing mass ratio of volatiles(VOLT*) to the second solvent (SOLV2*) ranges from 1 pound of volatiles(VOLT*) per 6 pounds of second solvent (SOLV2*), so this would be amixing mass ratio of 1/6 or 0.16; In embodiments, the mixing mass ratioof volatiles (VOLT*) to the second solvent (SOLV2*) ranges from 1 poundof volatiles (VOLT*) per 7 pounds of second solvent (SOLV2*), so thiswould be a mixing mass ratio of 1/7 or 0.14; In embodiments, the mixingmass ratio of volatiles (VOLT*) to the second solvent (SOLV2*) rangesfrom 1 pound of volatiles (VOLT*) per 8 pounds of second solvent(SOLV2*), so this would be a mixing mass ratio of 1/8 or 0.125; Inembodiments, the mixing mass ratio of volatiles (VOLT*) to the secondsolvent (SOLV2*) ranges from 1 pound of volatiles (VOLT*) per 9 poundsof second solvent (SOLV2*), so this would be a mixing mass ratio of 1/9or 0.11; In embodiments, the mixing mass ratio of volatiles (VOLT*) tothe second solvent (SOLV2*) ranges from 1 pound of volatiles (VOLT*) per10 pounds of second solvent (SOLV2*), so this would be a mixing massratio of 1/10 or 0.1; In embodiments, the mixing mass ratio of volatiles(VOLT*) to the second solvent (SOLV2*) ranges from 1 pound of volatiles(VOLT*) per 12 pounds of second solvent (SOLV2*), so this would be amixing mass ratio of 1/12 or 0.08; In embodiments, the mixing mass ratioof volatiles (VOLT*) to the second solvent (SOLV2*) ranges from 1 poundof volatiles (VOLT*) per 14 pounds of second solvent (SOLV2*), so thiswould be a mixing mass ratio of 1/14 or 0.07; In embodiments, the mixingmass ratio of volatiles (VOLT*) to the second solvent (SOLV2*) rangesfrom 1 pound of volatiles (VOLT*) per 16 pounds of second solvent(SOLV2*), so this would be a mixing mass ratio of 1/16 or 0.06; Inembodiments, the mixing mass ratio of volatiles (VOLT*) to the secondsolvent (SOLV2*) ranges from 1 pound of volatiles (VOLT*) per 20 poundsof second solvent (SOLV2*), so this would be a mixing mass ratio of 1/20or 0.05; In embodiments, the mixing mass ratio of volatiles (VOLT*) tothe second solvent (SOLV2*) ranges from 1 pound of volatiles (VOLT*) per60 pounds of second solvent (SOLV2*), so this would be a mixing massratio of 1/60 or 0.016; In embodiments, the mixing mass ratio ofvolatiles (VOLT*) to the second solvent (SOLV2*) ranges from 1 pound ofvolatiles (VOLT*) per 100 pounds of second solvent (SOLV2*), so thiswould be a mixing mass ratio of 1/100 or 0.01. In embodiments, themixing mass ratio of pounds of volatiles (VOLT*) per pounds of secondsolvent (SOLV2*) ranges from 0.01 to 1.

A volatiles and solvent mixture (SVSM*) is discharged from the interior(VSMSI*) of the volatiles and solvent mixing system (VSMS*). FIG. 17D′shows one non-limiting embodiment of the separation system (SEPSOL*).The separation system (SEPSOL*) is configured to separate the secondsolvent (SOLV2*) from the volatiles and solvent mixture (SVSM*). Theseparation system (SEPSOL*) is configured to evaporate at least aportion of the solvent (SOLV2*) from the volatiles and solvent mixture(SVSM*) to create concentrated volatiles (CVOLT*). Concentratedvolatiles (CVOLT*) have a reduced amount of second solvent (SOLV2*)relative to the volatiles and solvent mixture (SVSM*). The separationsystem (SEPSOL*) is configured to separate the second solvent (SOLV2*)from the volatiles and solvent mixture (SVSM*) to concentrate thevolatiles (VOLT*). In embodiments, concentrated volatiles (CVOLT*) aremixed with terpenes that were separated out in the volatiles extractionsystem (VES*). In embodiments, concentrated volatiles (CVOLT*) are mixedwith insects and/or insect lipids within the Insect ProductionSuperstructure System (IPSS) as disclosed in Volume I.

The separation system (SEPSOL*) is configured to separate the secondsolvent (SOLV2*) from the volatiles and solvent mixture (SVSM*) byevaporation, rotary evaporation, distillation, crystallization, vacuumflashing, or wiped film evaporation, wherein the distillation includes adistillation column, with trays, packing, or a wiper, or aspinning-band. In embodiments, a vacuum may be pulled on the separationsystem (SEPSOL*) to aide in evaporation of the second solvent (SOLV2*)from the volatiles and solvent mixture (SVSM*), as shown in FIG. 17D′.

In embodiments, the second solvent (SOLV2*) and volatiles (VOLT*) aremiscible. In embodiments, the second solvent (SOLV2*) and oil within thevolatiles (VOLT*) are miscible. In embodiments, the second solvent(SOLV2*) and terpenes within the volatiles (VOLT*) are miscible. Inembodiments, the second solvent (SOLV2*) and wax within the volatiles(VOLT*) are miscible. In embodiments, the second solvent (SOLV2*) andwax within the volatiles (VOLT*) are immiscible.

In instances where the second solvent (SOLV2*) and wax within thevolatiles (VOLT*) are immiscible, a solvent cooler (SOLV-C*) is providedto cool the volatiles and solvent mixture (SVSM*) that is evacuated fromthe interior (VSMSI*) of the volatiles and solvent mixing system(VSMS*). The solvent cooler (SOLV-C*) lowers the temperature of thevolatiles and solvent mixture (SVSM*) to permit phase separation of thewax from the volatiles (VOLT*). The volatiles and solvent mixture(SVSM*) is a reduced temperature second volatiles and solvent mixture(RTSVSM*) as it is leaves the solvent cooler (SOLV-C*). In embodiments,the solvent cooler (SOLV-C*) cools the filtered volatiles and ethanolmixture (VOLT**) to produce a chilled volatiles and ethanol mixture(VOLT1*).

In embodiments, the solvent cooler (SOLV-C*) operates at a temperaturerange including one or more ranges selected from the group consistingof: 32 degrees Fahrenheit to 0 degrees Fahrenheit, 0 degrees Fahrenheitto −10 degrees Fahrenheit, −10 degrees Fahrenheit to −20 degreesFahrenheit, −20 degrees Fahrenheit to −30 degrees Fahrenheit, −30degrees Fahrenheit to −40 degrees Fahrenheit, −40 degrees Fahrenheit to−50 degrees Fahrenheit, −50 degrees Fahrenheit to −75 degreesFahrenheit, −75 degrees Fahrenheit to −100 degrees Fahrenheit, −100degrees Fahrenheit to −125 degrees Fahrenheit, or −135 degreesFahrenheit to −150 degrees Fahrenheit. In embodiments, the solventcooler (SOLV-C*) operates at a temperature less than 50 degrees F. Inembodiments, the solvent cooler (SOLV-C*) operates at a temperature lessthan 40 degrees F. In embodiments, the solvent cooler (SOLV-C*) operatesat a temperature less than 30 degrees F. In embodiments, the solventcooler (SOLV-C*) operates at a temperature less than 20 degrees F. Inembodiments, the solvent cooler (SOLV-C*) operates at a temperature lessthan 10 degrees F. In embodiments, the solvent cooler (SOLV-C*) operatesat a temperature less than 00 degrees F. In embodiments, the reducedtemperature second volatiles and solvent mixture (RTSVSM*) leaves thesolvent cooler (SOLV-C*) at a temperature including one or more from thegroup consisting of: less than 50 degrees F., less than 40 degrees F.,less than 30 degrees F., less than 20 degrees F., less than 10 degreesF., and less than 0 degrees F.

In embodiments, a solvent filter (SOLV-F*) is configured to accept atleast a portion of the volatiles and solvent mixture (SVSM*) and/or thechilled volatiles and ethanol mixture (VOLT1*). In embodiments, asolvent filter (SOLV-F*) is configured to accept at least a portion ofthe reduced temperature second volatiles and solvent mixture (RTSVSM*).In embodiments, the solvent filter (SOLV-F*) is configured to separatewax (WAX*) from the volatiles and solvent mixture (SVSM*) and/or thechilled volatiles and ethanol mixture (VOLT1*). In embodiments, thesolvent filter (SOLV-F*) is configured to separate wax (WAX*) from thereduced temperature second volatiles and solvent mixture (RTSVSM*). Thesolvent filter (SOLV-F*) discharges a volatiles and solvent mixture(SVSM*)volatiles and solvent mixture (SVSM*) which may then be routed tothe separation system (SEPSOL*) of FIG. 17D′. In embodiments, the wax(WAX*) is mixed with insect lipids to make cosmetics, drugs, lip balm,and mixtures as disclosed in FIG. 12D of Volume I.

In embodiments, the wax separated in the solvent filter (SOLV-F*) isseparated under vacuum conditions. In embodiments, the vacuum conditionsare provided by a vacuum system, aspirator, eductor, or an ejector. Inembodiments, the aspirator is a type of ejector-jet pump, which producesvacuum by means of the Venturi effect. In embodiments, the wax separatedin the solvent filter (SOLV-F*) is filtered with filter paper. Inembodiments, the filter paper includes filter paper, polyethersulfone(PES) membrane filter, glass filter, polytetrafluoroethylene (PTFE)filter, quartz filter, or cellulose filter paper. In embodiments, thewax separated in the solvent filter (SOLV-F*) is filtered with a mixedcellulose ester membranes are comprised of cellulose acetate andcellulose nitrate. In embodiments, the wax separated in the solventfilter (SOLV-F*) wherein the solvent filter (SOLV-F*) includes poresizes ranging from between: 0.01 microns to 0.02 microns, 0.02 micronsto 0.03 microns, 0.03 microns to 0.04 microns, 0.04 microns to 0.05microns, 0.05 microns to 0.06 microns, 0.06 microns to 0.07 microns,0.07 microns to 0.08 microns, 0.08 microns to 0.09 microns, 0.09 micronsto 0.10 microns, 0.10 microns to 0.11 microns, 0.11 microns to 0.12microns, 0.12 microns to 0.13 microns, 0.13 microns to 0.14 microns,0.14 microns to 0.15 microns, 0.15 microns to 0.16 microns, 0.16 micronsto 0.17 microns, 0.17 microns to 0.18 microns, 0.18 microns to 0.19microns, 0.19 microns to 0.20 microns, 0.20 microns to 0.25 microns,0.25 microns to 0.30 microns, 0.30 microns to 0.35 microns, 0.35 micronsto 0.40 microns, 0.40 microns to 0.45 microns, 0.45 microns to 0.50microns, or 0.50 microns to 0.60 microns.

In embodiments, the wax separated in the solvent filter (SOLV-F*) has amelting point ranging including one or more melting point rangesselected from the group consisting of 75.00 degrees Fahrenheit 77.50Fahrenheit, 77.50 degrees Fahrenheit 80.00 Fahrenheit, 80.00 degreesFahrenheit 82.50 Fahrenheit, 82.50 degrees Fahrenheit 85.00 Fahrenheit,85.00 degrees Fahrenheit 87.50 Fahrenheit, 87.50 degrees Fahrenheit90.00 Fahrenheit, 90.00 degrees Fahrenheit 92.50 Fahrenheit, 92.50degrees Fahrenheit 95.00 Fahrenheit, 95.00 degrees Fahrenheit 97.50Fahrenheit, 97.50 degrees Fahrenheit 100.00 Fahrenheit, 100.00 degreesFahrenheit 102.50 Fahrenheit, 102.50 degrees Fahrenheit 105.00Fahrenheit, 105.00 degrees Fahrenheit 107.50 Fahrenheit, 107.50 degreesFahrenheit 110.00 Fahrenheit, 110.00 degrees Fahrenheit 112.50Fahrenheit, 112.50 degrees Fahrenheit 115.00 Fahrenheit, 115.00 degreesFahrenheit 117.50 Fahrenheit, 117.50 degrees Fahrenheit 120.00Fahrenheit, 120.00 degrees Fahrenheit 122.50 Fahrenheit, 122.50 degreesFahrenheit 125.00 Fahrenheit, 125.00 degrees Fahrenheit 127.50Fahrenheit, 127.50 degrees Fahrenheit 130.00 Fahrenheit, 130.00 degreesFahrenheit 132.50 Fahrenheit, 132.50 degrees Fahrenheit 135.00Fahrenheit, 135.00 degrees Fahrenheit 137.50 Fahrenheit, 137.50 degreesFahrenheit 140.00 Fahrenheit, 140.00 degrees Fahrenheit 142.50Fahrenheit, 142.50 degrees Fahrenheit 145.00 Fahrenheit, 145.00 degreesFahrenheit 147.50 Fahrenheit, 147.50 degrees Fahrenheit 150.00Fahrenheit, 150.00 degrees Fahrenheit 152.50 Fahrenheit, 152.50 degreesFahrenheit 155.00 Fahrenheit, 155.00 degrees Fahrenheit 157.50Fahrenheit, 157.50 degrees Fahrenheit 160.00 Fahrenheit, 160.00 degreesFahrenheit 162.50 Fahrenheit, 162.50 degrees Fahrenheit 165.00Fahrenheit, 165.00 degrees Fahrenheit 167.50 Fahrenheit, 167.50 degreesFahrenheit 170.00 Fahrenheit, 170.00 degrees Fahrenheit 172.50Fahrenheit, 172.50 degrees Fahrenheit 175.00 Fahrenheit, 175.00 degreesFahrenheit 177.50 Fahrenheit, or 177.50 degrees Fahrenheit 180.00Fahrenheit.

In embodiments, the wax separated in the solvent filter (SOLV-F*) isfurther mixed with one or more waxes selected from the group consistingof acacia decurrens flower cera (mimosa flower wax), almond wax, avocadowax, beery wax, bees wax, cananga odorata flower cera (ylang ylangflower wax), candelilla wax, Cannabis sativa oil, castor wax, cupuacubutter, floral wax, hemp wax, hydrogenated almond oil, hydrogenatedanimal-based oils, hydrogenated apricot kernel oil, hydrogenated avocadooil, hydrogenated brazil nut oil, hydrogenated canola oil, hydrogenatedcashew oil, hydrogenated cocoa butter, hydrogenated coconut oil,hydrogenated coffee oil, hydrogenated corn oil, hydrogenated cottonseedoil, hydrogenated grapeseed oil, hydrogenated hazelnut oil, hydrogenatedhemp oil, hydrogenated hop oil, hydrogenated insect oil, hydrogenatedlard oil, hydrogenated lard, hydrogenated macadamia nut oil,hydrogenated mustard oil, hydrogenated olive oil, hydrogenated palmkernel oil, hydrogenated palm oil, hydrogenated peanut oil, hydrogenatedpeppermint oil, hydrogenated rapeseed oil, hydrogenated rice bran oil,hydrogenated rice oil, hydrogenated safflower oil, hydrogenatedsemi-refined sesame oil, hydrogenated semi-refined sunflower oil,hydrogenated sesame oil, hydrogenated soybean oil, hydrogenated walnutoil, jasminum grandiflorum flower cera (jasmine flower wax), Lavandulaangustifolia flower cera (lavender flower wax), mmyrica fruit wax, olivewax, prunus amygdalus dulcis oil, rapeseed wax, rice bran wax, rosadamascene flower cera (rose flower wax), shea butter, soybean wax,sunflower wax, vegan wax, vegetable wax, wax from Mexican shrubEuphorbia antisyphilitica, and wax from the berries of rhus verniciflua.

In embodiments, the wax separated in the solvent filter (SOLV-F*) isused to make a consumer product, the consumer product includes waxseparated in the solvent filter (SOLV-F*) mixed with one or more waxesselected from the group consisting of acacia decurrens flower cera(mimosa flower wax), almond wax, avocado wax, beery wax, bees wax,cananga odorata flower cera (ylang ylang flower wax), candelilla wax,Cannabis sativa oil, castor wax, cupuacu butter, floral wax, hemp wax,hydrogenated almond oil, hydrogenated animal-based oils, hydrogenatedapricot kernel oil, hydrogenated avocado oil, hydrogenated brazil nutoil, hydrogenated canola oil, hydrogenated cashew oil, hydrogenatedcocoa butter, hydrogenated coconut oil, hydrogenated coffee oil,hydrogenated corn oil, hydrogenated cottonseed oil, hydrogenatedgrapeseed oil, hydrogenated hazelnut oil, hydrogenated hemp oil,hydrogenated hop oil, hydrogenated insect oil, hydrogenated lard oil,hydrogenated lard, hydrogenated macadamia nut oil, hydrogenated mustardoil, hydrogenated olive oil, hydrogenated palm kernel oil, hydrogenatedpalm oil, hydrogenated peanut oil, hydrogenated peppermint oil,hydrogenated rapeseed oil, hydrogenated rice bran oil, hydrogenated riceoil, hydrogenated safflower oil, hydrogenated semi-refined sesame oil,hydrogenated semi-refined sunflower oil, hydrogenated sesame oil,hydrogenated soybean oil, hydrogenated walnut oil, jasminum grandiflorumflower cera (jasmine flower wax), Lavandula angustifolia flower cera(lavender flower wax), mmyrica fruit wax, olive wax, prunus amygdalusdulcis oil, rapeseed wax, rice bran wax, rosa damascene flower cera(rose flower wax), shea butter, soybean wax, sunflower wax, vegan wax,vegetable wax, wax from Mexican shrub Euphorbia antisyphilitica, and waxfrom the berries of rhus verniciflua.

In embodiments, the wax separated in the solvent filter (SOLV-F*)includes a mixture of hydrocarbon molecules containing between twentyand fifty carbon atoms. In embodiments, the wax separated in the solventfilter (SOLV-F*) includes a mixture of hydrocarbon molecules containingbetween twenty and forty carbon atoms. In embodiments, the wax separatedin the solvent filter (SOLV-F*) includes an aliphatic ester. Inembodiments, the wax separated in the solvent filter (SOLV-F*) includesdiesters of 4-hydroxycinnamic acid. In embodiments, the wax separated inthe solvent filter (SOLV-F*) includes w-hydroxycarboxylic acids. Inembodiments, the wax separated in the solvent filter (SOLV-F*) includesfatty alcohols. In embodiments, the wax separated in the solvent filter(SOLV-F*) can be further processed by bleaching. In embodiments, the waxseparated in the solvent filter (SOLV-F*) can be further processed withhydrogen peroxide. In embodiments, the wax separated in the solventfilter (SOLV-F*) can be further processed with a mixture of water andhydrogen peroxide. In embodiments, the wax separated in the solventfilter (SOLV-F*) can be further processed with a mixture of treatedwater and hydrogen peroxide.

FIG. 17D′

FIG. 17D′ shows a separation system (SEPSOL*) that is configured toseparate at least a portion of the solvent (SOLV2*) and/or volatilesand/or cannabinoids from the volatiles and solvent mixture (SVSM*) toproduce concentrated volatiles (CVOLT*). FIG. 17D′ shows a separationsystem (SEPSOL*) that is configured to separate at least a portion ofthe psilocybin extract, psilocin extract, baeocystin extract, and/ornorbaeocystin extract from the volatiles and solvent mixture (SVSM*) toproduce concentrated volatiles (CVOLT*). In embodiments, the volatilesand solvent mixture (SVSM*) include psilocybin, psilocin, baeocystin,and/or norbaeocystin.

In embodiments, the separation system (SEPSOL*) includes an evaporator(J11*). FIG. 17D′ shows at least a portion of the volatiles and solventmixture (SVSM*) transferred to the separation system (SEPSOL*) from thevolatiles and solvent mixing system (VSMS*) shown in FIG. 17C′. Thevolatiles and solvent mixture (SVSM*) is transferred from the solventcooler (SOLV-C*) or from the solvent filter (SOLV-F*) of FIG. 17C′ tothe separation system (SEPSOL*) of FIG. 17D′.

FIG. 17D′ displays the separation system (SEPSOL*) as an evaporator(J11*) which separates or evaporates the second solvent (SOLV2*) fromthe volatiles and solvent mixture (SVSM*) to produce concentratedvolatiles (CVOLT*). In embodiments, the evaporator (J11*) is awiped-film evaporator (J11A*). In embodiments, the evaporator (J11*) iscomprised of one or more from the group consisting of a rotaryevaporator, falling film tubular evaporator, rising/falling film tubularevaporator, rising film tubular evaporator, forced circulationevaporator, internal pump forced circulation evaporator, plateevaporator, evaporative cooler, multiple-effect evaporator, thermalvapor recompression evaporator, mechanical vapor recompressionevaporator, flash tank, a crystallizer, a draft tube and bafflecrystallizer, cooling crystallization, evaporative crystallization,fractional crystallization, and a distillation column, wherein thedistillation includes a distillation column, with trays, packing, or awiper, or a spinning-band. In embodiments, the separation system(SEPSOL*) is a distillation system. In embodiments, the separationsystem (SEPSOL*) is short-path molecular distillation system.

In embodiments, the evaporator (J11*) includes a forced circulationevaporator including one or more from the group consisting of a fallingfilm tubular evaporator, rising/falling film tubular evaporator, risingfilm tubular evaporator, falling film evaporator, rising/falling filmevaporator, rising film evaporator, internal pump forced circulationevaporator, plate evaporator, evaporative cooler, multiple-effectevaporator, thermal vapor recompression evaporator, mechanical vaporrecompression evaporator, a crystallizer, a draft tube and bafflecrystallizer, cooling crystallization, evaporative crystallization,fractional crystallization, and a distillation column, wherein thedistillation includes a distillation column, with trays, packing, or awiper, or a spinning-band. In embodiments, the evaporator (J11*)includes a falling film tubular evaporator, rising/falling film tubularevaporator, rising film tubular evaporator, having a tube velocityranging from 5 to 10 feet per second (ft/s), 10 to 15 ft/s, 15 to 20ft/s, or 20 to 25 ft/s.

In embodiments, the distillation system include spinning banddistillation system which uses a spinning helical band made of an inertmaterial such as metal, Teflon, composites, or other materials to pushthe rising vapors and descending condensate to the sides of the column,coming into close contact with each other. In embodiments, thedistillation system include spinning band distillation system which usesa rotating helical band to create a high number of theoretical plates.

In embodiments, the distillation column includes a packed distillationcolumn including packing. In embodiments, the packing within the packeddistillation column includes structured packing or random packing. Inembodiments, the distillation column includes a vertically orientedcylindrical, or rectangular, pressure vessel having a lower section, andan upper section, along with a central section that contains packing ortrays. In embodiments, the packing within the packed distillation columnincludes raschig rings, pall rings, berl saddles, intalox packing, metalstructured grid packing, hollow spherical packing, high performancethermoplastic packing, structured packing, synthetic woven fabric, orceramic packing, or the like, wherein media is supported upon a suitablesupport grid system. In embodiments, the distillation column includestrays. In embodiments, the trays include valve trays, sieve trays, andbubble cap trays. In embodiments, the sieve trays have holes, whereinthe holes have a diameter ranging in size from 0.0625 to 0.125 inches,0.125 inches to 0.25 inches, 0.25 to 0.375 inches, or 0.375 inches to0.5 inches.

In embodiments, each trays includes a weir, wherein the weir heightranges from 0.25 to 0.5 inches, 0.5 to 0.75 inches, 0.75 to 1 inches, 1to 1.25 inches, 1.25 to 1.5 inches, 1.5 to 1.75 inches, 1.75 to 2inches, 2 to 3, 3 to 3.5 inches, or 3.5 to 4 inches. In embodiments, thedistillation column includes 2 to 3 trays, 3 to 4 trays, 4 to 5 trays, 5to 6 trays, 6 to 7 trays, 7 to 8 trays, 8 to 9 trays, 9 to 10 trays, 10to 15 trays, 15 to 20 trays, 20 to 30 trays, 30 to 40 trays, or 40 to 50trays. In embodiments, the pressure drop across each tray ranges from0.025 to 0.05 pounds per square inch (PSI), 0.05 to 0.075 PSI, 0.075 to0.1 PSI, 0.1 to 0.125 PSI, 0.125 to 0.105 PSI, 0.105 to 0.175 PSI, 0.175to 0.2 PSI, 0.2 to 0.3 PSI. In embodiments, the distillation columnincludes a tray spacing ranging from 2 to 4 inches, 4 to 6 inches, 6 to8 inches, 8 to 10 inches, 10 to 12 inches, 12 to 14 inches, 14 to 16inches, 16 to 18 inches, or 18 to 20 inches, wherein the tray spacing isthe vertical height between trays within the distillation column.

In embodiments, the distillation column includes a liquid rate of 0.25to 0.5 gpm/ft2 (gallons per minute per square foot), 0.5 to 1 gpm/ft2, 1to 2 gpm/ft2, 2 to 3 gpm/ft2, 3 to 4 gpm/ft2, 4 to 5 gpm/ft2, 5 to 10gpm/ft2, 10 to 15 gpm/ft2, 15 to 20 gpm/ft2, 20 to 25 gpm/ft2, or 25 to30 gpm/ft2. In embodiments, the distillation column includes a reflux tofeed ratio ranging from 0.1 to 0.2 mol/mol, 0.2 to 0.3 mol/mol, 0.3 to0.4 mol/mol, 0.4 to 0.5 mol/mol, 0.5 to 0.6 mol/mol, 0.6 to 0.7 mol/mol,0.7 to 0.8 mol/mol, or 0.8 to 0.9 mol/mol. In embodiments, thedistillation column includes a reflux ratio ranging from 1 to 1.1, 1.2to 1.2, 1.2 to 1.3, 1.3 to 1.4, 1.4 to 1.5, 1.5 to 1.6, 1.6 to 1.7, 1.7to 1.8, 1.8 to 1.9, or 1.9 to 2.0. In embodiments, the velocity throughthe trays within the distillation column include 0.5 to 1 feet persecond (ft/s), 1 to 1.5 ft/s, 1.5 to 2 ft/s, 2 to 2.5 ft/s, 2.5 to 3ft/s, 3 to 3.5 ft/s, 3.5 to 4 ft/s, 4 to 4.5 ft/s, 4.5 to 5 ft/s, 5 to5.5 ft/s, 5.5 to 6 ft/s, 6 to 7 ft/s, 7 to 8 ft/s, 8 to 9 ft/s, or 9 to10 ft/s.

In embodiments, when referring to the evaporator and/or the rotaryevaporator in this disclosure, the evaporator and/or rotary evaporatormay include one or more selected from the group consisting of: anevaporator and/or rotary evaporator provided by: BUCHI Labortechnik AG;Eyela Tokyo Rikakikai Co. Ltd; Heidolph Instruments Gmbh & Co. KG.; IKAWorks, Inc.; KNF Neuberger, Inc.; Labfirst Scientific Instruments(Shanghai) Co., Ltd.; Xi'an Yuanjian Instrument Equipment Co., Ltd.;Labtech S.R.L.; Hydrion Scientific Instruments Co., Ltd.; Shanghai HJLab Instruments Co., Ltd.; Stewart Equipment Co Inc.; Thermo FisherScientific, Fisher Clinical Services Inc; or Cole Parmer Instrument CoLtd.

In embodiments, when referring to the rotary evaporator in thisdisclosure, the rotary evaporator may include one or more evaporationflask volumes selected from the group consisting of: 1 liter to 2liters, 2 liters to 3 liters, 3 liters to 4 liters, 4 liters to 5liters, 5 liter to 10 liters, 10 liters to 20 liters, 20 liters to 30liters, 30 liters to 40 liters, or 40 liters to 50 liters.

In embodiments, the throughput of concentrated volatiles (CVOLT*)includes one or more throughputs selected from the group consisting of:0.1 pounds per day to 0.2 pounds per day, 0.2 pounds per day to 0.4pounds per day, 0.4 pounds per day to 0.8 pounds per day, 0.8 pounds perday to 1.0 pounds per day, 1 pounds per day to 2 pounds per day, 2pounds per day to 4 pounds per day, 4 pounds per day to 8 pounds perday, 8 pounds per day to 16 pounds per day, 16 pounds per day to 32pounds per day, 32 pounds per day to 64 pounds per day, 64 pounds perday to 128 pounds per day, 128 pounds per day to 256 pounds per day, 256pounds per day to 512 pounds per day, 512 pounds per day to 1024 poundsper day, 1024 pounds per day to 2048 pounds per day, 2048 pounds per dayto 4096 pounds per day, 4096 pounds per day to 8192 pounds per day, 8192pounds per day to 16384 pounds per day, 16384 pounds per day to 32768pounds per day, 32768 pounds per day to 65536 pounds per day, 65536pounds per day to 131072 pounds per day, 131072 pounds per day to 262144pounds per day, 262144 pounds per day to 524288 pounds per day, 524288pounds per day to 1048576 pounds per day, 1048576 pounds per day to2097152 pounds per day, and 2097152 pounds per day to 4194304 pounds perday.

In embodiments, the FSS produces cannabis at a rate of: 0.5 tons per dayto 1 tons per day, 1 tons per day to 2 tons per day, 2 tons per day to 4tons per day, 4 tons per day to 8 tons per day, 8 tons per day to 16tons per day, 16 tons per day to 25 tons per day, 25 tons per day to 50tons per day, 50 tons per day to 75 tons per day, 75 tons per day to 100tons per day, 100 tons per day to 150 tons per day, 150 tons per day to200 tons per day, 200 tons per day to 250 tons per day, 250 tons per dayto 300 tons per day, 300 tons per day to 350 tons per day, 350 tons perday to 400 tons per day, 400 tons per day to 450 tons per day, 450 tonsper day to 500 tons per day, 500 tons per day to 600 tons per day, 600tons per day to 700 tons per day, 700 tons per day to 800 tons per day,800 tons per day to 900 tons per day, 900 tons per day to 1000 tons perday, 1000 tons per day to 1500 tons per day, 1500 tons per day to 2000tons per day, 2000 tons per day to 2500 tons per day, 2500 tons per dayto 3000 tons per day, 3000 tons per day to 3500 tons per day, 3500 tonsper day to 4000 tons per day, 4000 tons per day to 4500 tons per day,4500 tons per day to 5000 tons per day, 5000 tons per day to 6000 tonsper day, 6000 tons per day to 7000 tons per day, 7000 tons per day to8000 tons per day, 8000 tons per day to 9000 tons per day, or 9000 tonsper day to 10000 tons per day.

The evaporator (J11*) shown in FIG. 17D′ is that of a wiped-filmevaporator (J11A*). The evaporator (J11*) has a vapor inlet (J12*), aninput (J16*), a heating jacket (J17*), a first output (J18*), and asecond output (J19*). In embodiments, the evaporator (J11*) iselectrically heated. In embodiments, the vapor inlet (J12*) is providedwith a vapor (J12A*) such as steam. The vapor inlet is connected to avapor supply conduit (J13*). A vapor supply valve (J14*) is positionedon the vapor supply conduit (J13*). The vapor supply valve (J14*) isequipped with a controller (J15A*) that is configured to input andoutput a signal (J15B*) to the computer (COMP). In embodiments, thepressure drop across the vapor supply valve (J14*) ranges from between 5PSI to 10 PSI, 15 PSI to 25 PSI, 25 PSI to 35 PSI, 35 PSI to 45 PSI, 45PSI to 55 PSI, 55 PSI to 65 PSI, 65 PSI to 75 PSI, 75 PSI to 85 PSI. Inembodiments, the vapor supply valve (J14*) percent open during normaloperation ranges from 10% open to 25% open, 25% open to 35% open, 35%open to 45% open, 45% open to 55% open, 55% open to 65% open, 65% opento 75% open, 75% open to 80% open. In embodiment, the volatiles andsolvent mixture (SVSM*) transferred from the solvent filter (SOLV-F*) isheated with a heat exchanger (JDHK) before being introduced to theseparation system (SEPSOL*). In embodiments, the heat exchanger (JDHK)tetrahydrocannabinolic acid within the solvent mixture to decarboxylatethe tetrahydrocannabinolic acid to form active tetrahydrocannabinol. Inembodiments, tetrahydrocannabinolic acid within the solvent mixture maybe decarboxylated to form active tetrahydrocannabinol before the solventis separated by vacuum evaporation and after filtration to remove thewax.

A separated vapor transfer conduit (J20*) is connected to the firstoutput (J18*) and is configured to transfer vaporized solvent (J22*)from the evaporator (J11*) to a condenser (J26*). In embodiments, thevaporized solvent (J22*) is the second solvent (SOLV2*) in vapor phase.When the second solvent (SOLV2*) is evaporated or vaporized into avaporized solvent (J22*) the concentration of the volatiles (VOLT*)within the volatiles and solvent mixture (SVSM*) increases to formconcentrated volatiles (CVOLT*).

The condenser (J26*) has a vaporized liquid input (J25*) that isconfigured to transfer the vaporized solvent (J22*) or vaporized secondsolvent (SOLV2*) from the separated vapor transfer conduit (J20*) to thecondenser (J26*). The condenser (J26*) is configured to accept vaporizedsolvent (J22*) from the evaporator (J11*) and condense the liquid intocondensate (J27*). Condensate (J27*) is discharged from the condenser(J26*) via a condenser condensate output (J30*). The condensate (J27*)is the second solvent (SOLV2*) which can then be recovered and reused inthe volatiles and solvent mixing system (VSMS*).

The condenser is connected to a vacuum system (J32*) via a gas/vaportransfer conduit (J33*). Gas/vapor (J35*) is evacuated from thecondenser (J27*) via a gas/vapor discharge (J37*). The gas/vapor (J35*)transferred from the condenser (J26*) to the vacuum system (J32*) may becomprised of one or more from the group consisting of second solvent,carbon dioxide, nitrogen, air, steam, water vapor, and non-condensables.The vacuum system (J32*) may be any conceivable system configured todraw a vacuum on the condenser (J26*). In embodiments, the vacuum system(J32*) is that of a liquid-ring vacuum pump. A portion of the gas/vapor(J35*) may be in turn condensed within the vacuum system (J26*). Aportion of the gas/vapor (J35*) may be discharged from the vacuum system(J26*) via a gas/vapor transfer line (J39*).

In embodiments, the vacuum system (J32*) pulls a vacuum on theevaporator (J11*) at a pressure ranging from 0.25 pounds per square inchabsolute (PSIA) to 0.05 PSIA to 0.5 PSIA, 0.5 PSIA, 0.5 PSIA to 1 PSIA,1 PSIA to 1.5 PSIA, 1.5 PSIA to 3 PSIA, 3 PSIA to 4.5 PSIA, 4.5 PSIA to6 PSIA, 6 PSIA to 7.5 PSIA, 7.5 PSIA to 9 PSIA, 9 PSIA to 10.5 PSIA,10.5 PSIA to 12 PSIA, 12 PSIA to 13.5 PSIA, 12 PSIA to 12.25 PSIA, 12.25PSIA to 12.5 PSIA, 12.5 PSIA to 12.75 PSIA, 12.75 PSIA to 13 PSIA, 13PSIA to 13.25 PSIA, 13.25 PSIA to 13.5 PSIA, 13.5 PSIA to 13.75 PSIA,13.75 PSIA to 14 PSIA, 14 PSIA to 14.25 PSIA, 14.25 PSIA to 14.5 PSIA,or 14.5 PSIA to 14.75 PSIA.

The condenser (J26*) is provided with a coolant input (J36*) and acoolant output (J40*). The coolant input (J36*) is configured to accepta coolant supply (J38*) and the coolant output (J40*) is configured todischarge a coolant return (J42′*). The coolant supply (J38*) isconfigured to reduce the temperature of the vaporized solvent (J22*)within the condenser (J26*) to convert the vaporized solvent (J22*) intoa liquid condensate (J27*). In embodiments, the coolant includes treatedwater and a mixture of

In embodiments, the coolant includes water. In embodiments, the coolantincludes a mixture of treated water and glycerol, ethanol, methanol,glycerol, ethylene glycol, a glycol, propylene glycol, an alcohol,anti-freeze fluid, or a water-based synthetic liquid. In embodiments,the anti-freeze fluid includes mono ethylene glycol, or ono propyleneglycol. In embodiments, the coolant includes a corrosion inhibitor.

In embodiments, a chiller (J26**) reciprocates the coolant from thecondenser to the chiller to maintain a constant temperature within thecondenser (J26*) to convert the vaporized solvent (J22*) into a liquidcondensate (J27*). In embodiments, the liquid condensate (J27*)condensed in the condenser is reused in the cannabis solvent extractionprocess. In embodiments, the chiller (J26**) provides a coolant to thecondenser (J26*), wherein the coolant has a temperature entering thecoolant input (J36*) of the condenser (J26*) at a temperature rangingfrom 60 degrees Fahrenheit to 40 degrees Fahrenheit, 40 degreesFahrenheit to 32 degrees Fahrenheit, 32 degrees Fahrenheit to 0 degreesFahrenheit, 0 degrees Fahrenheit to −10 degrees Fahrenheit, −10 degreesFahrenheit to −20 degrees Fahrenheit, −20 degrees Fahrenheit to −30degrees Fahrenheit, −30 degrees Fahrenheit to −40 degrees Fahrenheit,−40 degrees Fahrenheit to −50 degrees Fahrenheit, −50 degrees Fahrenheitto −75 degrees Fahrenheit, −75 degrees Fahrenheit to −100 degreesFahrenheit, −100 degrees Fahrenheit to −125 degrees Fahrenheit, or −135degrees Fahrenheit to −150 degrees Fahrenheit. In embodiments, a coldtrap (J32**) is installed in between the gas/vapor discharge (J37*) ofthe condenser (J26*) and the vacuum system (J32*). The cold trap (J32**)condenses any additional vapor within the gas/vapor (J35*) so that nocondensation occurs in the vacuum system (J26*). In embodiments, a coldtrap (J32**) is installed in between the gas/vapor discharge (J37*) ofthe condenser (J26*) and the vacuum system (J32*). The cold trap (J32**)condenses any additional vapor within the gas/vapor (J35*) so that nocondensation occurs in the vacuum system (J26*) to as to maximize therecovery of solvent within to reuse in the extraction of cannabinoidsfrom the cannabis. In embodiments, a cold trap (J32**) includes dry iceand a solvent, wherein the dry ice contacts the gas/vapor (J35*) tocondense solvent. In embodiments, a cold trap (J32**) includes dry iceand a solvent, wherein the solvent includes one or more selected fromthe group consisting of glycerol, ethanol, methanol, glycerol, ethyleneglycol, a glycol, propylene glycol, an alcohol, anti-freeze fluid, or awater-based synthetic liquid.

The evaporator (J11*) has an evaporator condensate output (J24*) forevacuating condensate (J41*) from the heating jacket (J17*). Thecondensate (J41*) discharged via the evaporator condensate output (J24*)was provided to the evaporator heating jacket (J17*) as the vapor(J12A*) or steam. The heating jacket (J17*) accepts a source of vapor(J12A*), and evaporates second solvent (SOLV2*) from the volatiles andsolvent mixture (SVSM*) to form vaporized solvent (J22*) that isdischarged from the evaporator (J11*) and sent to the condenser (J26*).

The heating jacket (J17*) accepts a source of vapor (J12A*), andevaporates second solvent (SOLV2*) from the volatiles and solventmixture (SVSM*) to form concentrates volatiles (CVOLT*) that has areduced amount of second solvent (SOLV2*) relative to the volatiles andsolvent mixture (SVSM*).

In embodiments, the evaporator (J11*) takes the form of a wiped-filmevaporator (J11A*). In embodiments, the wiped-film evaporator (J11A*)has a motor (J42*) and a wiper (J44*). In embodiments, the motor (J42*)and wiper (J44*) act together to wipe at least one heat transfer surfacewithin the evaporator (J11*).

The input (J16*) is configured to introduce the volatiles and solventmixture (SVSM*) to the evaporator (J11*). In embodiments, the evaporatorvaporizes the second solvent (SOLV2*) from within the volatiles andsolvent mixture (SVSM*) to produce a vaporized solvent (J22*) andconcentrated volatiles (CVOLT*).

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing a source of cannabis;    -   (b) after step (a), grinding the cannabis to form ground        cannabis;    -   (c) after step (b), extracting volatiles from the ground        cannabis with a first solvent to form a first solvent and        volatiles mixture; and    -   (d) after step (c), separating at least a portion of the        volatiles from the first solvent and volatiles mixture;        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1*) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor; In embodiments, the first solvent        (SOLV1*) includes one or more from the group consisting of        petroleum ether, pentane, n-hexane, hexanes, diethyl ether,        ethyl acetate, and ethanol.

the terpenes include one or more from the group consisting of limonene,humulene, pinene, linalool, caryophyllene, myrcene, eucalyptol,nerolidol, bisablol, and phytol.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing DANLEO III or cannabis;    -   (b) grinding DANLEO III or cannabis after step (a);    -   (c) extracting volatiles (VOLT*) from DANLEO III or cannabis        after step (b) with a first solvent (SOLV1*) to form a first        solvent and volatiles mixture (FSVM*);    -   (d) separating at least a portion of the volatiles (VOLT*) from        the first solvent and volatiles mixture (FSVM*);    -   (e) mixing the volatiles with a second solvent (SOLV2*) after        step (d) to form a volatiles and solvent mixture (SVSM*);    -   (f) cooling the volatiles and solvent mixture (SVSM*) after step        (e);    -   (g) filtering the volatiles and solvent mixture (SVSM*); and    -   (h) evaporating the second solvent (SOLV2*) from the volatiles        and solvent mixture (SVSM*);        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1*) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2*) includes one or more from the group        consisting of petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing DANLEO III or cannabis;    -   (b) grinding DANLEO III or cannabis after step (a); and    -   (c) extracting volatiles (VOLT*) from DANLEO III or cannabis        after step (b) with a first solvent (SOLV1*) to form a first        solvent and volatiles mixture (FSVM*);    -   (d) separating at least a portion of the volatiles (VOLT*) from        the first solvent and volatiles mixture (FSVM*);    -   (e) mixing the volatiles with a second solvent (SOLV2*) after        step (d) to form a volatiles and solvent mixture (SVSM*);    -   (f) separating at least a portion of the volatiles (VOLT*) from        the second solvent (SOLV2*);        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1*) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor; the second solvent (SOLV2*) includes one        or more from the group consisting of a petroleum ether, pentane,        n-hexane, hexanes, diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing DANLEO III or cannabis;    -   (b) grinding DANLEO III or cannabis after step (a);    -   (c) extracting volatiles (VOLT*) from DANLEO III or cannabis        after step (b) with a first solvent (SOLV1*) to form a first        solvent and volatiles mixture (FSVM*);    -   (d) separating at least a portion of the volatiles (VOLT*) from        the first solvent and volatiles mixture (FSVM*);    -   (e) mixing a portion of the volatiles (VOLT*) after step (d)        with insects;        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1*) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor; the second solvent (SOLV2*) includes one        or more from the group consisting of petroleum ether, pentane,        n-hexane, hexanes, diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol;        the insects are comprised of one or more from the group        consisting of Orthoptera order of insects, grasshoppers,        crickets, cave crickets, Jerusalem crickets, katydids, weta,        lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,        worms, bees, centipedes, cockroaches, dragonflies, beetles,        scorpions, tarantulas, termites, insect lipids, and insect oil,        or any insects or insect products mentioned herein.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing DANLEO III or cannabis;    -   (b) grinding DANLEO III or cannabis after step (a);    -   (c) extracting volatiles (VOLT*) from DANLEO III or cannabis        after step (b) with a first solvent (SOLV1*) to form a first        solvent and volatiles mixture (FSVM*);    -   (d) separating at least a portion of the volatiles (VOLT*) from        the first solvent and volatiles mixture (FSVM*);    -   (e) mixing the volatiles (VOLT*) with a second solvent (SOLV2*)        after step (d) to form a volatiles and solvent mixture (SVSM*);    -   (f) separating at least a portion of the volatiles (VOLT*) from        the volatiles and solvent mixture (SVSM*);    -   (g) mixing a portion of the volatiles (VOLT*) after step (f)        with insects;        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1*) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2*) includes one or more from the group        consisting of petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol.        the insects are comprised of one or more from the group        consisting of Orthoptera order of insects, grasshoppers,        crickets, cave crickets, Jerusalem crickets, katydids, weta,        lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,        worms, bees, centipedes, cockroaches, dragonflies, beetles,        scorpions, tarantulas, termites, insect lipids, and insect oil,        or any insects or insect products mentioned herein.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing DANLEO III or cannabis;    -   (b) grinding DANLEO III or cannabis after step (a); and    -   (c) extracting volatiles (VOLT*) from DANLEO III or cannabis        after step (b) with a first solvent (SOLV1*) to form a first        solvent and volatiles mixture (FSVM*);    -   (d) separating at least a portion of the volatiles (VOLT*) from        the first solvent and volatiles mixture (FSVM*);    -   (e) mixing the volatiles (VOLT*) with a second solvent (SOLV2*)        after step (d) to form a volatiles and solvent mixture (SVSM*);    -   (f) evaporating at least a portion of the second solvent        (SOLV2*) from the volatiles and solvent mixture (SVSM*) to        create concentrated volatiles (CVOLT*) that have reduced amount        of second solvent relative to the volatiles and solvent mixture        (SVSM*);    -   (g) mixing a portion of the volatiles (VOLT*) after step (f)        with insects;        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1*) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2*) includes one or more from the group        consisting of a petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol;        the insects are comprised of one or more from the group        consisting of Orthoptera order of insects, grasshoppers,        crickets, cave crickets, Jerusalem crickets, katydids, weta,        lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,        worms, bees, centipedes, cockroaches, dragonflies, beetles,        scorpions, tarantulas, termites, insect lipids, and insect oil.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first water treatment unit (A1*) including a cation            configured to remove positively charged ions from water to            form a positively charged ion depleted water (06A*), the            positively charged ions are comprised of one or more from            the group consisting of calcium, magnesium, sodium, and            iron;        -   (a2) a second water treatment unit (A2*) including an anion            configured to remove negatively charged ions from the            positively charged ion depleted water (06A*) to form a            negatively charged ion depleted water (09A*), the negatively            charged ions are comprised of one or more from the group            consisting of iodine, chloride, and sulfate;        -   (a3) an optional third water treatment unit (A3*) including            a membrane configured to remove undesirable compounds from            the negatively charged ion depleted water (09A*) to form an            undesirable compounds depleted water (12A*), the undesirable            compounds are comprised of one or more from the group            consisting of dissolved organic chemicals, viruses,            bacteria, and particulates;        -   (a4) an enclosure (ENC*) having an interior (ENC1*);        -   (a5) a plurality of growing assemblies (100*, 200*)            positioned within the interior (ENC1*) of the enclosure            (ENC*), each growing assembly (100*, 200*) configured to            grow DANLEO III (107*, 207*) or cannabis (107*, 207*);        -   (a6) a plurality of lights (L1*, L2*) configured to            illuminate the interior (ENC1*) of the enclosure (ENC*);        -   (a7) a volatiles extraction system (VES*) that is configured            to separate volatiles (VOLT*) from DANLEO III (107*, 207*)            or cannabis (107*, 207*) with use of a first solvent            (SOLV1*), the volatiles extraction system (VES*) has an            interior (VESI*) that is configured to contain DANLEO III            (107*, 207*) or cannabis (107*, 207*), the volatiles            extraction system (VES*) is configured to accept a first            solvent (SOLV1*), the first solvent (SOLV1*) is configured            to contact the DANLEO III (107*, 207*) or cannabis (107*,            207*) within the interior (VESI*) of the volatiles            extraction system (VES*), the volatiles extraction system            (VES*) outputs a first solvent and volatiles mixture            (FSVM*);        -   (a8) a first solvent separation system (SSS) that is            configured to separate the volatiles (VOLT) from the first            solvent and volatiles mixture (FSVM), the first solvent            separation system (SSS) has an interior (SSSI), the first            solvent and volatiles mixture (FSVM) is transferred from the            interior (VESI) of the volatiles extraction system (VES) to            the interior (SSSI) of the first solvent separation system            (SSS), the first solvent separation system (SSS) outputs a            volatiles (VOLT) and a separated first solvent (SOLV1-S);        -   (a9) a volatiles and solvent mixing system (VSMS) that is            configured to mix the volatiles (VOLT) with a second solvent            (SOLV2), the volatiles (VOLT) that are introduced to the            interior (VSMSI) of the volatiles and solvent mixing system            (VSMS) are transferred from the volatiles extraction systems            (VES), a second volatiles and solvent mixture (SVSM) is            discharged from the interior (VSMSI) of the volatiles and            solvent mixing system (VSMS);        -   (a10) a second solvent separation system (SEPSOL) that is            configured to separate at least a portion of the second            solvent (SOLV2) from the second volatiles and solvent            mixture (SVSM) to produce concentrated volatiles (CVOLT);    -   (b) providing a source of water;    -   (c) removing positively charged ions and negatively charged ions        and optionally undesirable compounds from the water of step (b);    -   (d) mixing the water after step (c) with macro-nutrients,        micro-nutrients, or a pH adjustment solution to form a liquid        mixture;    -   (e) pressurizing the liquid mixture after step (d) to form a        pressurized liquid mixture;    -   (f) transferring the pressurized liquid mixture of step (e) to        the plurality of growing assemblies; and    -   (g) illuminating the plurality of growing assemblies (100, 200)        with the plurality of lights;    -   (h) growing DANLEO III or cannabis within the plurality of        growing assemblies after step (g);    -   (i) harvesting DANLEO III or cannabis after growing DANLEO III        or cannabis in step (h);    -   (j) grinding DANLEO III or cannabis after step (i); and    -   (k) extracting volatiles (VOLT*) from DANLEO III or cannabis        after step (j) with a first solvent (SOLV1*) to form a first        solvent and volatiles mixture (FSVM*);    -   (l) separating at least a portion of the volatiles (VOLT*) from        the first solvent and volatiles mixture (FSVM*);    -   (m) mixing the volatiles (VOLT*) with a second solvent (SOLV2*)        after step (1) to form a volatiles and solvent mixture (SVSM*);    -   (n) cooling the volatiles and solvent mixture (SVSM*) after step        (m);    -   (o) filtering the volatiles and solvent mixture (SVSM*) after        step (n);    -   (p) evaporating the second solvent (SOLV2*) from the second        volatiles and solvent mixture (SVSM);        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes; the first solvent (SOLV1*) includes one or        more from the group consisting of acetone, alcohol, oil, butane,        butter, carbon dioxide, coconut oil, ethanol, gas, gaseous        carbon dioxide, hexane, insect lipids, isobutane, isopropanol,        liquid carbon dioxide, liquid, naphtha, olive oil, pentane,        propane, R134 refrigerant gas, subcritical carbon dioxide,        supercritical carbon dioxide, vapor; the second solvent (SOLV2*)        includes one or more from the group consisting of a petroleum        ether, pentane, n-hexane, hexanes, diethyl ether, ethyl acetate,        and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing a farming superstructure system (FSS), including:    -   (a1) a cation configured to remove positively charged ions from        water to form a positively charged ion depleted water (06A), the        positively charged ions are comprised of one or more from the        group consisting of calcium, magnesium, sodium, and iron;    -   (a2) an anion configured to remove negatively charged ions from        the positively charged ion depleted water (06A) to form a        negatively charged ion depleted water (09A), the negatively        charged ions are comprised of one or more from the group        consisting of iodine, chloride, and sulfate;    -   (a3) a membrane configured to remove undesirable compounds from        the negatively charged ion depleted water (09A) to form an        undesirable compounds depleted water (12A), the undesirable        compounds are comprised of one or more from the group consisting        of dissolved organic chemicals, viruses, bacteria, and        particulates;    -   (a4) an enclosure (ENC) having an interior (ENC1);    -   (a5) a plurality of growing assemblies (100, 200) positioned        within the interior (ENC1) of the enclosure (ENC), each growing        assembly (100, 200) configured to grow DANLEO III (107, 207) or        cannabis (107, 207);    -   (a6) a plurality of lights (L1, L2) configured to illuminate the        interior (ENC1) of the enclosure (ENC);    -   (a7) a volatiles extraction system (VES) that is configured to        separate volatiles (VOLT) from DANLEO III (107, 207) or cannabis        (107, 207) with use of a first solvent (SOLV1), the volatiles        extraction system (VES) has an interior (VEST) that is        configured to contain DANLEO III (107, 207) or cannabis (107,        207), the volatiles extraction system (VES) is configured to        accept a first solvent (SOLV1), the first solvent (SOLV1) is        configured to contact the DANLEO III (107, 207) or cannabis        (107, 207) within the interior (VEST) of the volatiles        extraction system (VES), the volatiles extraction system (VES)        outputs a first solvent and volatiles mixture (FSVM);    -   (a8) a first solvent separation system (SSS) that is configured        to separate the volatiles (VOLT) from the first solvent and        volatiles mixture (FSVM), the first solvent separation system        (SSS) has an interior (SSSI), the first solvent and volatiles        mixture (FSVM) is transferred from the interior (VEST) of the        volatiles extraction system (VES) to the interior (SSSI) of the        first solvent separation system (SSS), the first solvent        separation system (SSS) outputs a volatiles (VOLT) and a        separated first solvent (SOLV1-S);    -   (a9) a volatiles and solvent mixing system (VSMS) that is        configured to mix the volatiles (VOLT) with a second solvent        (SOLV2), the volatiles (VOLT) that are introduced to the        interior (VSMSI) of the volatiles and solvent mixing system        (VSMS) are transferred from the volatiles extraction systems        (VES), a second volatiles and solvent mixture (SVSM) is        discharged from the interior (VSMSI) of the volatiles and        solvent mixing system (VSMS);    -   (a10) a second solvent separation system (SEPSOL) that is        configured to separate at least a portion of the second solvent        (SOLV2) from the second volatiles and solvent mixture (SVSM) to        produce concentrated volatiles (CVOLT);    -   (b) providing a source of water;    -   (c) removing positively charged ions and negatively charged ions        and optionally undesirable compounds from the water of step (b);    -   (d) mixing the water after step (c) with macro-nutrients,        micro-nutrients, or a pH adjustment solution to form a liquid        mixture;    -   (e) pressurizing the liquid mixture after step (d) to form a        pressurized liquid mixture;    -   (f) transferring the pressurized liquid mixture of step (e) to        the plurality of growing assemblies; and    -   (g) illuminating the plurality of growing assemblies (100, 200)        with the plurality of lights (L1, L2);    -   (h) growing DANLEO III or cannabis within the plurality of        growing assemblies after step (g);    -   (i) harvesting DANLEO III or cannabis after growing DANLEO III        or cannabis in step (h);    -   (j) grinding DANLEO III or cannabis after step (i); and    -   (k) extracting volatiles (VOLT) from DANLEO III or cannabis        after step (j) with a first solvent (SOLV1) to form a first        solvent and volatiles mixture (FSVM);    -   (l) separating at least a portion of the volatiles (VOLT) from        the first solvent and volatiles mixture (FSVM);    -   (m) mixing a portion of the volatiles (VOLT) after step (1) with        insects;        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2) includes one or more from the group        consisting of a petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol;        the insects are comprised of one or more from the group        consisting of Orthoptera order of insects, grasshoppers,        crickets, cave crickets, Jerusalem crickets, katydids, weta,        lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,        worms, bees, centipedes, cockroaches, dragonflies, beetles,        scorpions, tarantulas, termites, insect lipids, and insect oil,        or any insects or insect products mentioned herein.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first water treatment unit (A1) including a cation            configured to remove positively charged ions from water to            form a positively charged ion depleted water (06A), the            positively charged ions are comprised of one or more from            the group consisting of calcium, magnesium, sodium, and            iron;        -   (a2) a second water treatment unit (A2) including an anion            configured to remove negatively charged ions from the            positively charged ion depleted water (06A) to form a            negatively charged ion depleted water (09A), the negatively            charged ions are comprised of one or more from the group            consisting of iodine, chloride, and sulfate;        -   (a3) an optional third water treatment unit (A3) including a            membrane configured to remove undesirable compounds from the            negatively charged ion depleted water (09A) to form an            undesirable compounds depleted water (12A), the undesirable            compounds are comprised of one or more from the group            consisting of dissolved organic chemicals, viruses,            bacteria, and particulates;        -   (a4) an enclosure (ENC) having an interior (ENC1);        -   (a5) a plurality of growing assemblies (100, 200) positioned            within the interior (ENC1) of the enclosure (ENC), each            growing assembly (100, 200) configured to grow DANLEO III            (107, 207) or cannabis (107, 207);        -   (a6) a plurality of lights (L1, L2) configured to illuminate            the interior (ENC1) of the enclosure (ENC);        -   (a7) a volatiles extraction system (VES) that is configured            to separate volatiles (VOLT) from DANLEO III (107, 207) or            cannabis (107, 207) with use of a first solvent (SOLV1), the            volatiles extraction system (VES) has an interior (VESI)            that is configured to contain DANLEO III (107, 207) or            cannabis (107, 207), the volatiles extraction system (VES)            is configured to accept a first solvent (SOLV1), the first            solvent (SOLV1) is configured to contact the DANLEO III            (107, 207) or cannabis (107, 207) within the interior (VESI)            of the volatiles extraction system (VES), the volatiles            extraction system (VES) outputs a first solvent and            volatiles mixture (FSVM);        -   (a8) a first solvent separation system (SSS) that is            configured to separate the volatiles (VOLT) from the first            solvent and volatiles mixture (FSVM), the first solvent            separation system (SSS) has an interior (SSSI), the first            solvent and volatiles mixture (FSVM) is transferred from the            interior (VEST) of the volatiles extraction system (VES) to            the interior (SSSI) of the first solvent separation system            (SSS), the first solvent separation system (SSS) outputs a            volatiles (VOLT) and a separated first solvent (SOLV1-S);        -   (a9) a volatiles and solvent mixing system (VSMS) that is            configured to mix the volatiles (VOLT) with a second solvent            (SOLV2), the volatiles (VOLT) that are introduced to the            interior (VSMSI) of the volatiles and solvent mixing system            (VSMS) are transferred from the volatiles extraction systems            (VES), a second volatiles and solvent mixture (SVSM) is            discharged from the interior (VSMSI) of the volatiles and            solvent mixing system (VSMS);        -   (a10) a second solvent separation system (SEPSOL) that is            configured to separate at least a portion of the second            solvent (SOLV2) from the second volatiles and solvent            mixture (SVSM) to produce concentrated volatiles (CVOLT);    -   (b) providing a source of water;    -   (c) removing positively charged ions and negatively charged ions        and optionally undesirable compounds from the water of step (b);    -   (d) mixing the water after step (c) with macro-nutrients,        micro-nutrients, or a pH adjustment solution to form a liquid        mixture;    -   (e) pressurizing the liquid mixture after step (d) to form a        pressurized liquid mixture;    -   (f) transferring the pressurized liquid mixture of step (e) to        the plurality of growing assemblies;    -   and    -   (g) illuminating the plurality of growing assemblies (100, 200)        with the plurality of lights (L1, L2);    -   (h) growing DANLEO III or cannabis within the plurality of        growing assemblies after step (g);    -   (i) harvesting DANLEO III or cannabis after growing DANLEO III        or cannabis in step (h);    -   (j) grinding DANLEO III or cannabis after step (i); and    -   (k) extracting volatiles (VOLT) from DANLEO III or cannabis        after step (j) with a first solvent (SOLV1) to form a first        solvent and volatiles mixture (FSVM);    -   (l) separating at least a portion of the volatiles (VOLT) from        the first solvent and volatiles mixture (FSVM);    -   (m) mixing the volatiles with a second solvent (SOLV2) after        step (1) to form a second volatiles and solvent mixture (SVSM);        and    -   (n) separating at least a portion of the volatiles (VOLT) from        the second volatiles and solvent mixture (SVSM);        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2) includes one or more from the group        consisting of a petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first water treatment unit (A1) including a cation            configured to remove positively charged ions from water to            form a positively charged ion depleted water (06A), the            positively charged ions are comprised of one or more from            the group consisting of calcium, magnesium, sodium, and            iron;        -   (a2) a second water treatment unit (A2) including an anion            configured to remove negatively charged ions from the            positively charged ion depleted water (06A) to form a            negatively charged ion depleted water (09A), the negatively            charged ions are comprised of one or more from the group            consisting of iodine, chloride, and sulfate;        -   (a3) an optional third water treatment unit (A3) including a            membrane configured to remove undesirable compounds from the            negatively charged ion depleted water (09A) to form an            undesirable compounds depleted water (12A), the undesirable            compounds are comprised of one or more from the group            consisting of dissolved organic chemicals, viruses,            bacteria, and particulates;        -   (a4) an enclosure (ENC) having an interior (ENC1);        -   (a5) a plurality of growing assemblies (100, 200) positioned            within the interior (ENC1) of the enclosure (ENC), each            growing assembly (100, 200) configured to grow DANLEO III            (107, 207) or cannabis (107, 207);        -   (a6) a plurality of lights (L1, L2) configured to illuminate            the interior (ENC1) of the enclosure (ENC);        -   (a7) a volatiles extraction system (VES) that is configured            to separate volatiles (VOLT) from DANLEO III (107, 207) or            cannabis (107, 207) with use of a first solvent (SOLV1), the            volatiles extraction system (VES) has an interior (VEST)            that is configured to contain DANLEO III (107, 207) or            cannabis (107, 207), the volatiles extraction system (VES)            is configured to accept a first solvent (SOLV1), the first            solvent (SOLV1) is configured to contact the DANLEO III            (107, 207) or cannabis (107, 207) within the interior (VEST)            of the volatiles extraction system (VES), the volatiles            extraction system (VES) outputs a first solvent and            volatiles mixture (FSVM);        -   (a8) a first solvent separation system (SSS) that is            configured to separate the volatiles (VOLT) from the first            solvent and volatiles mixture (FSVM), the first solvent            separation system (SSS) has an interior (SSSI), the first            solvent and volatiles mixture (FSVM) is transferred from the            interior (VEST) of the volatiles extraction system (VES) to            the interior (SSSI) of the first solvent separation system            (SSS), the first solvent separation system (SSS) outputs a            volatiles (VOLT) and a separated first solvent (SOLV1-S);        -   (a9) a volatiles and solvent mixing system (VSMS) that is            configured to mix the volatiles (VOLT) with a second solvent            (SOLV2), the volatiles (VOLT) that are introduced to the            interior (VSMSI) of the volatiles and solvent mixing system            (VSMS) are transferred from the volatiles extraction systems            (VES), a second volatiles and solvent mixture (SVSM) is            discharged from the interior (VSMSI) of the volatiles and            solvent mixing system (VSMS);        -   (a10) a second solvent separation system (SEPSOL) that is            configured to separate at least a portion of the second            solvent (SOLV2) from the second volatiles and solvent            mixture (SVSM) to produce concentrated volatiles (CVOLT);    -   (b) providing a source of water;    -   (c) removing positively charged ions and negatively charged ions        and optionally undesirable compounds from the water of step (b);    -   (d) mixing the water after step (c) with macro-nutrients,        micro-nutrients, or a pH adjustment solution to form a liquid        mixture;    -   (e) pressurizing the liquid mixture after step (d) to form a        pressurized liquid mixture;    -   (f) transferring the pressurized liquid mixture of step (e) to        the plurality of growing assemblies; and    -   (g) illuminating the plurality of growing assemblies (100, 200)        with the plurality of lights (L1, L2);    -   (h) growing DANLEO III or cannabis within the plurality of        growing assemblies after step (g);    -   (i) harvesting DANLEO III or cannabis after growing DANLEO III        or cannabis in step (h);    -   (j) grinding DANLEO III or cannabis after step (i); and    -   (k) extracting volatiles (VOLT) from DANLEO III or cannabis        after step (j) with a first solvent (SOLV1) to form a first        solvent and volatiles mixture (FSVM);    -   (l) separating at least a portion of the volatiles (VOLT) from        the first solvent and volatiles mixture (FSVM);    -   (m) mixing the volatiles with a second solvent (SOLV2) after        step (1) to form a second volatiles and solvent mixture (SVSM);        and    -   (n) evaporating at least a portion of the second solvent (SOLV2)        from the second volatiles and solvent mixture (SVSM);        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2) includes one or more from the group        consisting of a petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol.

In embodiments, the present disclosure describes a method to separatevolatiles from cannabis, the method includes:

-   -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first water treatment unit (A1) including a cation            configured to remove positively charged ions from water to            form a positively charged ion depleted water (06A), the            positively charged ions are comprised of one or more from            the group consisting of calcium, magnesium, sodium, and            iron;        -   (a2) a second water treatment unit (A2) including an anion            configured to remove negatively charged ions from the            positively charged ion depleted water (06A) to form a            negatively charged ion depleted water (09A), the negatively            charged ions are comprised of one or more from the group            consisting of iodine, chloride, and sulfate;        -   (a3) an optional third water treatment unit (A3) including a            membrane configured to remove undesirable compounds from the            negatively charged ion depleted water (09A) to form an            undesirable compounds depleted water (12A), the undesirable            compounds are comprised of one or more from the group            consisting of dissolved organic chemicals, viruses,            bacteria, and particulates;        -   (a4) an enclosure (ENC) having an interior (ENC1);        -   (a5) a plurality of growing assemblies (100, 200) positioned            within the interior (ENC1) of the enclosure (ENC), each            growing assembly (100, 200) configured to grow DANLEO III            (107, 207) or cannabis (107, 207);        -   (a6) a plurality of lights (L1, L2) configured to illuminate            the interior (ENC1) of the enclosure (ENC);        -   (a7) a volatiles extraction system (VES) that is configured            to separate volatiles (VOLT) from DANLEO III (107, 207) or            cannabis (107, 207) with use of a first solvent (SOLV1), the            volatiles extraction system (VES) has an interior (VESI)            that is configured to contain DANLEO III (107, 207) or            cannabis (107, 207), the volatiles extraction system (VES)            is configured to accept a first solvent (SOLV1), the first            solvent (SOLV1) is configured to contact the DANLEO III            (107, 207) or cannabis (107, 207) within the interior (VEST)            of the volatiles extraction system (VES), the volatiles            extraction system (VES) outputs a first solvent and            volatiles mixture (FSVM);        -   (a8) a first solvent separation system (SSS) that is            configured to separate the volatiles (VOLT) from the first            solvent and volatiles mixture (FSVM), the first solvent            separation system (SSS) has an interior (SSSI), the first            solvent and volatiles mixture (FSVM) is transferred from the            interior (VEST) of the volatiles extraction system (VES) to            the interior (SSSI) of the first solvent separation system            (SSS), the first solvent separation system (SSS) outputs a            volatiles (VOLT) and a separated first solvent (SOLV1-S);        -   (a9) a volatiles and solvent mixing system (VSMS) that is            configured to mix the volatiles (VOLT) with a second solvent            (SOLV2), the volatiles (VOLT) that are introduced to the            interior (VSMSI) of the volatiles and solvent mixing system            (VSMS) are transferred from the volatiles extraction systems            (VES), a second volatiles and solvent mixture (SVSM) is            discharged from the interior (VSMSI) of the volatiles and            solvent mixing system (VSMS);        -   (a10) a second solvent separation system (SEPSOL) that is            configured to separate at least a portion of the second            solvent (SOLV2) from the second volatiles and solvent            mixture (SVSM) to produce concentrated volatiles (CVOLT);    -   (b) providing a source of water;    -   (c) removing positively charged ions and negatively charged ions        and optionally undesirable compounds from the water of step (b);    -   (d) mixing the water after step (c) with macro-nutrients,        micro-nutrients, or a pH adjustment solution to form a liquid        mixture;    -   (e) pressurizing the liquid mixture after step (d) to form a        pressurized liquid mixture;    -   (f) transferring the pressurized liquid mixture of step (e) to        the plurality of growing assemblies; and    -   (g) illuminating the plurality of growing assemblies (100, 200)        with the plurality of lights (L1, L2);    -   (h) growing DANLEO III or cannabis within the plurality of        growing assemblies after step (g);    -   (i) harvesting DANLEO III or cannabis after growing DANLEO III        or cannabis in step (h);    -   (j) grinding DANLEO III or cannabis after step (i); and    -   (k) extracting volatiles (VOLT) from DANLEO III or cannabis        after step (j) with a first solvent (SOLV1) to form a first        solvent and volatiles mixture (FSVM);    -   (l) separating at least a portion of the volatiles (VOLT) from        the first solvent and volatiles mixture (FSVM);    -   (m) mixing the volatiles with a second solvent (SOLV2) after        step (1) to form a second volatiles and solvent mixture (SVSM);    -   (n) separating at least a portion of the volatiles (VOLT) from        the second volatiles and solvent mixture (SVSM); and    -   (o) mixing a portion of the volatiles (VOLT) after step (n) with        insects;        wherein:        the volatiles include one or more from the group consisting of        oil, wax, terpenes;        the first solvent (SOLV1) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the second solvent (SOLV2) includes one or more from the group        consisting of a petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol;        the terpenes include one or more from the group consisting of        limonene, humulene, pinene, linalool, caryophyllene, myrcene,        eucalyptol, nerolidol, bisablol, and phytol;        the insects are comprised of one or more from the group        consisting of Orthoptera order of insects, grasshoppers,        crickets, cave crickets, Jerusalem crickets, katydids, weta,        lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,        worms, bees, centipedes, cockroaches, dragonflies, beetles,        scorpions, tarantulas, termites, insect lipids, and insect oil,        or any insects or insect products mentioned herein.        In embodiments, the present disclosure describes a method to        separate volatiles from cannabis, the method includes:    -   (a) providing a farming superstructure system (FSS), including:        -   (a1) a first water treatment unit (A1) including a cation            configured to remove positively charged ions from water to            form a positively charged ion depleted water (06A), the            positively charged ions are comprised of one or more from            the group consisting of calcium, magnesium, sodium, and            iron;        -   (a2) a second water treatment unit (A2) including an anion            configured to remove negatively charged ions from the            positively charged ion depleted water (06A) to form a            negatively charged ion depleted water (09A), the negatively            charged ions are comprised of one or more from the group            consisting of iodine, chloride, and sulfate;        -   (a3) an optional third water treatment unit (A3) including a            membrane configured to remove undesirable compounds from the            negatively charged ion depleted water (09A) to form an            undesirable compounds depleted water (12A), the undesirable            compounds are comprised of one or more from the group            consisting of dissolved organic chemicals, viruses,            bacteria, and particulates;        -   (a4) an enclosure (ENC) having an interior (ENC1);        -   (a5) a plurality of growing assemblies (100, 200) positioned            within the interior (ENC1) of the enclosure (ENC), each            growing assembly (100, 200) configured to grow DANLEO III            (107, 207) or cannabis (107, 207);        -   (a6) a plurality of lights (L1, L2) configured to illuminate            the interior (ENC1) of the enclosure (ENC);        -   (a7) a volatiles extraction system (VES) that is configured            to separate volatiles (VOLT) from DANLEO III (107, 207) or            cannabis (107, 207) with use of a first solvent (SOLV1), the            volatiles extraction system (VES) has an interior (VESI)            that is configured to contain DANLEO III (107, 207) or            cannabis (107, 207), the volatiles extraction system (VES)            is configured to accept a first solvent (SOLV1), the first            solvent (SOLV1) is configured to contact the DANLEO III            (107, 207) or cannabis (107, 207) within the interior (VESI)            of the volatiles extraction system (VES), the volatiles            extraction system (VES) outputs a first solvent and            volatiles mixture (FSVM);        -   (a8) a first solvent separation system (SSS) that is            configured to separate the volatiles (VOLT) from the first            solvent and volatiles mixture (FSVM), the first solvent            separation system (SSS) has an interior (SSSI), the first            solvent and volatiles mixture (FSVM) is transferred from the            interior (VEST) of the volatiles extraction system (VES) to            the interior (SSSI) of the first solvent separation system            (SSS), the first solvent separation system (SSS) outputs a            volatiles (VOLT) and a separated first solvent (SOLV1-S);        -   (a9) a volatiles and solvent mixing system (VSMS) that is            configured to mix the volatiles (VOLT) with a second solvent            (SOLV2), the volatiles (VOLT) that are introduced to the            interior (VSMSI) of the volatiles and solvent mixing system            (VSMS) are transferred from the volatiles extraction systems            (VES), a second volatiles and solvent mixture (SVSM) is            discharged from the interior (VSMSI) of the volatiles and            solvent mixing system (VSMS);        -   (a10) a second solvent separation system (SEPSOL) that is            configured to separate at least a portion of the second            solvent (SOLV2) from the second volatiles and solvent            mixture (SVSM) to produce concentrated volatiles (CVOLT);    -   (b) providing a source of water;    -   (c) removing positively charged ions and negatively charged ions        and optionally undesirable compounds from the water of step (b);    -   (d) mixing the water after step (c) with macro-nutrients,        micro-nutrients, or a pH adjustment solution to form a liquid        mixture;    -   (e) pressurizing the liquid mixture after step (d) to form a        pressurized liquid mixture;    -   (f) transferring the pressurized liquid mixture of step (e) to        the plurality of growing assemblies; and    -   (g) illuminating the plurality of growing assemblies (100, 200)        with the plurality of lights (L1, L2);    -   (h) growing DANLEO III or cannabis within the plurality of        growing assemblies after step (g);    -   (i) harvesting DANLEO III or cannabis after growing DANLEO III        or cannabis in step (h);    -   (j) grinding DANLEO III or cannabis after step (i); and    -   (k) extracting volatiles (VOLT) from DANLEO III or cannabis        after step (j) with a first solvent (SOLV1) to form a first        solvent and volatiles mixture (FVSM);    -   (l) separating at least a portion of the volatiles (VOLT) from        the first solvent and volatiles mixture (FVSM); and    -   (m) mixing a portion of the volatiles (VOLT) after step (1) with        insects;        wherein:        the first solvent (SOLV1) includes one or more from the group        consisting of acetone, alcohol, oil, butane, butter, carbon        dioxide, coconut oil, ethanol, gas, gaseous carbon dioxide,        hexane, insect lipids, isobutane, isopropanol, liquid carbon        dioxide, liquid, naphtha, olive oil, pentane, propane, R134        refrigerant gas, subcritical carbon dioxide, supercritical        carbon dioxide, vapor;        the insects are comprised of one or more from the group        consisting of Orthoptera order of insects, grasshoppers,        crickets, cave crickets, Jerusalem crickets, katydids, weta,        lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,        worms, bees, centipedes, cockroaches, dragonflies, beetles,        scorpions, tarantulas, termites, insect lipids, and insect oil,        or any insects or insect products mentioned herein.        In embodiments, the present disclosure describes a method to        separate and concentrate volatiles from cannabis, the method        includes:    -   (a) providing cannabis;    -   (b) grinding cannabis after step (a);    -   (c) separating volatiles (VOLT) from cannabis after step (b)        with a first solvent (SOLV1) to form a first solvent and        volatiles mixture (FSVM);    -   (d) separating volatiles (VOLT) from the first solvent and        volatiles mixture (FSVM);    -   (e) mixing the volatiles with a second solvent (SOLV2) after        step (d) to form a second volatiles and solvent mixture (SVSM);    -   (h) separating the second solvent (SOLV2) from the second        volatiles and solvent mixture (SVSM);        wherein:        the first solvent (SOLV1) includes one or more from the group        consisting of butane, carbon dioxide, gas, gaseous carbon        dioxide, hexane, insect lipids, isobutane, isopropanol, liquid        carbon dioxide, naphtha, pentane, propane, R134 refrigerant gas,        subcritical carbon dioxide, supercritical carbon dioxide, vapor;        the second solvent (SOLV2) includes one or more from the group        consisting of a petroleum ether, pentane, n-hexane, hexanes,        diethyl ether, ethyl acetate, and ethanol.

In embodiments, the method to separate and concentrate volatiles fromcannabis, also includes: (e) mixing a portion of the volatiles (VOLT*)after step (d) with insects; wherein: the insects are comprised of oneor more from the group consisting of Orthoptera order of insects,grasshoppers, crickets, cave crickets, Jerusalem crickets, katydids,weta, lubber, acrida, locusts, cicadas, ants, mealworms, agave worms,worms, bees, centipedes, cockroaches, dragonflies, beetles, scorpions,tarantulas, termites, insect lipids, and insect oil, black soldier flylarvae, or any insects or insect products mentioned herein.

In embodiments, the method to separate and concentrate volatiles fromcannabis, also includes: (f) cooling the volatiles and solvent mixture(SVSM*) after step (e); and (g) filtering the volatiles and solventmixture (SVSM*).

In embodiments, the method to separate and concentrate volatiles fromcannabis, also includes: in step (c), separating volatiles (VOLT*) fromcannabis using a method that includes: (1) separating terpenes from thecannabis at a first temperature and a first pressure; and (2) separatingoil and wax from the cannabis at a second temperature and a secondpressure; wherein: the second temperature is greater than the firsttemperature; the second pressure is greater than the first pressure; theterpenes include one or more from the group consisting of limonene,humulene, pinene, linalool, caryophyllene, myrcene, eucalyptol,nerolidol, bisablol, and phytol; the volatiles include one or more fromthe group consisting of oil, wax, terpenes, and tetrahydrocannabinol(THC). The volatiles includes tetrahydrocannabinol (THC).

In embodiments, an analyzer (J70′) is used to analyze the concentratedvolatiles (CVOLT*), the analyzer (J70′) includes one or more analyzersselected from the group consisting of liquid chromatography-massspectrometry, gas chromatography-mass spectrometry (GC-MS), andinductively coupled plasma mass spectrometry (ICP-MS). In embodiments,the analyzer (J70′) is used to detect for the presence of solvents,mycotoxins, microbes, moisture content, metals, pesticides, terpenes,and potency.

In embodiments, the concentrated volatiles (CVOLT*) includes: a nitrate(NO3) concentration having a maximum level of 1,000 mg NO3/kg ofend-product; a mycotoxin analysis including: an ochratoxin Aconcentration having a maximum level of 10 μg/kg of end-product; adeoxynivalenol concentration having a maximum level of 2,000 μg/kg ofend-product; a zearalenone concentration having a maximum level of 275μg/kg of end-product; a fumonisins concentration having a maximum levelof 2,500 μg/kg of end-product; a metals analysis including: a leadconcentration having a maximum level of 0.5 mg/kg of end-product; acadmium concentration having a maximum level of 0.5 mg/kg ofend-product; a mercury concentration having a maximum level of 0.5 mg/kgof end-product; a 3-monochloropropane-1,2-diol (3-MCPD) concentrationhaving a maximum level of 20 μg/kg of end-product; a dioxins andpolychlorinated biphenyls (PCBs) concentration having a maximum level of3 picogram/gram; a polycyclic aromatic hydrocarbon concentration havinga maximum level of 5 μg/kg of end-product; a benzo(a)pyreneconcentration having a maximum level of 2 or 5 μg/kg of end-product; atotal concentration of benzo(a)pyrene, benz(a)anthracene,benzo(b)fluoranthene and chrysene having a maximum level of 15 or 30μg/kg of end-product.

In embodiments, the insect traceability system includes a qualityanalysis of an that includes: a standard plate count (to test for totalaerobic bacterial and total mold and yeasts) having less than: 500,000colony forming unit per gram, 400,000 colony forming units per gram,300,000 colony forming units per gram, 200,000 colony forming units pergram, 100,000 colony forming units per gram, 50,000 colony forming unitsper gram, 25,000 colony forming units per gram, or 5,000 colony formingunits per gram; a coliform content less than 500 colony forming unitsper gram, 400 colony forming units per gram, 300 colony forming unitsper gram, 200 colony forming units per gram, 100 colony forming unitsper gram, 90 colony forming units per gram, 80 colony forming units pergram, 70 colony forming units per gram, 60 colony forming units pergram, 50 colony forming units per gram, 40 colony forming units pergram, 30 colony forming units per gram, 20 colony forming units pergram, or 10 colony forming units per gram; a coliform content less than500,000 colony forming unit per gram, 400,000 colony forming units pergram, 300,000 colony forming units per gram, 200,000 colony formingunits per gram, 100,000 colony forming units per gram, 50,000 colonyforming units per gram, 25,000 colony forming units per gram, or 5,000colony forming units per gram; a spore-forming sulphite reducinganaerobe content less than 500 colony forming units per gram, 400 colonyforming units per gram, 300 colony forming units per gram, 200 colonyforming units per gram, 100 colony forming units per gram, 90 colonyforming units per gram, 80 colony forming units per gram, 70 colonyforming units per gram, 60 colony forming units per gram, 50 colonyforming units per gram, 40 colony forming units per gram, 30 colonyforming units per gram, 20 colony forming units per gram, or 10 colonyforming units per gram; a spore-forming sulphite reducing anaerobecontent less than 500,000 colony forming unit per gram, 400,000 colonyforming units per gram, 300,000 colony forming units per gram, 200,000colony forming units per gram, 100,000 colony forming units per gram,50,000 colony forming units per gram, 25,000 colony forming units pergram, or 5,000 colony forming units per gram; a Pseudomonas aeruginosacontent less than 500 colony forming units per gram, 400 colony formingunits per gram, 300 colony forming units per gram, 200 colony formingunits per gram, 100 colony forming units per gram, 90 colony formingunits per gram, 80 colony forming units per gram, 70 colony formingunits per gram, 60 colony forming units per gram, 50 colony formingunits per gram, 40 colony forming units per gram, 30 colony formingunits per gram, 20 colony forming units per gram, or 10 colony formingunits per gram; a Pseudomonas aeruginosa content less than 500,000colony forming unit per gram, 400,000 colony forming units per gram,300,000 colony forming units per gram, 200,000 colony forming units pergram, 100,000 colony forming units per gram, 50,000 colony forming unitsper gram, 25,000 colony forming units per gram, or 5,000 colony formingunits per gram; a E. coli content less than 500 colony forming units pergram, 400 colony forming units per gram, 300 colony forming units pergram, 200 colony forming units per gram, 100 colony forming units pergram, 90 colony forming units per gram, 80 colony forming units pergram, 70 colony forming units per gram, 60 colony forming units pergram, 50 colony forming units per gram, 40 colony forming units pergram, 30 colony forming units per gram, 20 colony forming units pergram, or 10 colony forming units per gram; a E. coli content less than500,000 colony forming unit per gram, 400,000 colony forming units pergram, 300,000 colony forming units per gram, 200,000 colony formingunits per gram, 100,000 colony forming units per gram, 50,000 colonyforming units per gram, 25,000 colony forming units per gram, or 5,000colony forming units per gram.

In embodiments, the concentrated volatiles may be mixed with one or morewaxes selected from the group consisting of almond oil, animal-basedoils, apricot kernel oil, avocado oil, brazil nut oil, butter, canolaoil, cashew oil, cocoa butter, coconut oil, cooking oil, corn oil,cottonseed oil, fish oil, grapeseed oil, hazelnut oil, hemp oil, insectoil, lard, lard oil, macadamia nut oil, mustard oil, olive oil, palmkernel oil, palm oil, peanut oil, rapeseed oil, rice oil, rice bran oil,safflower oil, semi-refined sesame oil, semi-refined sunflower oil,sesame oil, soybean oil, tallow of beef, tallow of mutton, vegetableoil, and walnut oil.

In embodiments, the concentrated volatiles may be mixed with one or morewaxes selected from the group consisting of acacia decurrens flower cera(mimosa flower wax), almond wax, avocado wax, beery wax, bees wax,cananga odorata flower cera (ylang ylang flower wax), candelilla wax,Cannabis sativa oil, castor wax, cupuacu butter, floral wax, hemp wax,hydrogenated almond oil, hydrogenated animal-based oils, hydrogenatedapricot kernel oil, hydrogenated avocado oil, hydrogenated brazil nutoil, hydrogenated canola oil, hydrogenated cashew oil, hydrogenatedcocoa butter, hydrogenated coconut oil, hydrogenated coffee oil,hydrogenated corn oil, hydrogenated cottonseed oil, hydrogenatedgrapeseed oil, hydrogenated hazelnut oil, hydrogenated hemp oil,hydrogenated hop oil, hydrogenated insect oil, hydrogenated lard oil,hydrogenated lard, hydrogenated macadamia nut oil, hydrogenated mustardoil, hydrogenated olive oil, hydrogenated palm kernel oil, hydrogenatedpalm oil, hydrogenated peanut oil, hydrogenated peppermint oil,hydrogenated rapeseed oil, hydrogenated rice bran oil, hydrogenated riceoil, hydrogenated safflower oil, hydrogenated semi-refined sesame oil,hydrogenated semi-refined sunflower oil, hydrogenated sesame oil,hydrogenated soybean oil, hydrogenated walnut oil, jasminum grandiflorumflower cera (jasmine flower wax), Lavandula angustifolia flower cera(lavender flower wax), mmyrica fruit wax, olive wax, prunus amygdalusdulcis oil, rapeseed wax, rice bran wax, rosa damascene flower cera(rose flower wax), shea butter, soybean wax, sunflower wax, vegan wax,vegetable wax, wax from Mexican shrub Euphorbia antisyphilitica, and waxfrom the berries of rhus verniciflua.

In embodiments, the concentrated volatiles may be mixed with allspiceberries, almond meal, anise seed, annato seed, arrowroot powder, basil,bay leaves, black pepper, buttermilk, capsaicin, caraway, cayenne,celery seed, cheese cultures, chervil, chile powder, chives, cilantro,cinnamon, citric acid, cloves, coconut shredded, coriander, corn oil,corn starch, cream of tartar, cubeb berries, cumin, curry, dextrose,dill, enzymes, fennel, fenugreek, file powder, garlic powder, ginger,grapefruit peel, green peppercorns, honey, horseradish powder, juniperberries, kaffir lime, lavender, lemon grass powder, lemon peel, limepeel, long pepper, marjoram, molasses, mustard, natural smoke flavor,nigella seeds, nutmeg, onion powder, orange peel, oregano, paprika,parsley, peppermint, poppy seed, powdered cheese, red pepper, rosepetals, rosemary, saffron, sassafrass, sage, salt, savory, sesame seed,star anise, sugar, sugar maple, sumac, tamarind, tangerine peel,tarragon, thyme, tomatillo powder, tomato powder, turmeric, vanillaextract, wasabi powder, whey, or white peppercorns.

In embodiments, the concentrated volatiles may be mixed with serotonin,psilocybin, psilocin, baeocystin, lysergic acid diethylamide (LSD), ormescaline. In embodiments, the concentrated volatiles may be mixed withpsilocybin mushrooms and/or the alimentary composition. In embodiments,the concentrated volatiles may be mixed with psilocybin extract,psilocin extract, baeocystin extract, and/or norbaeocystin extract. Inembodiments, the concentrated volatiles may be mixed with milk, milkpowder, whole milk powder, goat milk, soy milk, almond milk, coconutmilk, oat milk, rice milk, cashew milk, macadamia milk, whole milk, 2%milk, 1% milk, organic milk, lactose-free milk, half and half, cream,buttermilk, or chocolate milk.

In embodiments, the concentrated volatiles may be further processed tocreate foodstuffs not only including ada, bagels, baked goods, biscuits,bitterballen, bonda, breads, cakes, candies, cereals, chips, chocolatebars, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crêpes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, poffertjes, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,specialty milk, tele-bhaja, tempura, toffee, tortillas, totopo, turkishdelights, or waffles.

In embodiments, the foodstuff includes a fiber-starch material, abinding agent, a moisture improving textural supplement, a densityimproving textural supplement, and/or insects. In embodiments, thefiber-starch materials may be comprised of singular or mixtures ofcereal-grain-based materials, grass-based materials, nut-basedmaterials, powdered fruit materials, root-based materials, tuber-basedmaterials, or vegetable-based materials. In embodiments, the bindingagents may be comprised of singular or mixtures of agar, agave, alginin,aspartame, arrowroot, carrageenan, collagen, cornstarch, egg whites,finely ground seeds, furcellaran, gelatin, guar gum, honey, katakuristarch, locust bean gum, pectin, potato starch, proteins, psylliumhusks, sago, sugars, stevia, syrups, tapioca, vegetable gums, or xanthangum. In embodiments, the moisture improving textural supplements may becomprised of singular or mixtures of almonds, brazil nuts, cacao,cashews, chestnuts, coconut, filberts, hazelnuts, Indian nuts, macadamianuts, nut butters, nut oils, nut powders, peanuts, pecans, pili nuts,pine nuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tigernuts, walnuts, and oils extracted from any one of the aforesaid nuts andnuts listed herein and combinations thereof. In embodiments, the insectsmay be Orthoptera order of insects including grasshoppers, crickets,cave crickets, Jerusalem crickets, katydids, weta, lubber, acrida, andlocusts. However, other orders of insects, such as cicadas, ants,mealworms, agave worms, worms, bees, centipedes, cockroaches,dragonflies, beetles, scorpions, tarantulas, termites, insect lipids,and insect oil, black soldier fly larvae, or any insects or insectproducts mentioned herein may be used as well. In embodiments, thedensity improving textural supplement may be comprised of singular ormixtures of extracted arrowroot starch, extracted corn starch, extractedlentil starch, extracted potato starch, or extracted tapioca starch.

In embodiments, the concentrated volatiles may be mixed withalpha-tocopherol, ascorbic acid, biotin, caffeine, calciferol, calcium,carotene, chloride, choline, chromium, citicoline, cobalamin, copper,fluoride, folacin, folate, folic acid, glucuronic acid, iodine, iron,L-phenylalanine, magnesium, malic acid, manganese, menadione, mineral,molybdenum, N-acetyl L tyrosine, niacin, pantothenic acid, phosphorus,phylloquinone, potassium, pyridoxine, retinal, retinoic acid, retinoids,retinol, retinyl esters, riboflavin, selenium, sodium, sulfur, taurine,thiamine, Vitamin A, Vitamin B1, vitamin B12, Vitamin B2, vitamin B3,vitamin B5, vitamin B6, vitamin B9, vitamin C, vitamin D, Vitamin E,vitamin H, vitamin K, or zinc. In embodiments, each serving size of thefoodstuff includes a cannabidiol content in milligrams per servingranging from 0 milligrams to 0.5 milligrams, 0.5 milligrams to 1milligrams, 1 milligrams to 1.5 milligrams, 1.5 milligrams to 2milligrams, 2 milligrams to 2.5 milligrams, 2.5 milligrams to 3milligrams, 3 milligrams to 3.5 milligrams, 3.5 milligrams to 4milligrams, 4 milligrams to 4.5 milligrams, 4.5 milligrams to 5milligrams, 5 milligrams to 5.5 milligrams, 5.5 milligrams t 6milligrams, 6 milligrams to 6.5 milligrams, 6.5 milligrams to 7milligrams, 7 milligrams to 7.5 milligrams, 7.5 milligrams to 8milligrams, 8 milligrams to 8.5 milligrams, 8.5 milligrams to 9milligrams, 9 milligrams to 9.5 milligrams, 9.5 milligrams to 10milligrams, 10 milligrams to 11 milligrams, 11 milligrams to 12milligrams, 12 milligrams to 13 milligrams, 13 milligrams to 14milligrams, 14 milligrams to 15 milligrams, 15 milligrams to 16milligrams, 16 milligrams to 17 milligrams, 17 milligrams to 18milligrams, 18 milligrams to 19 milligrams, 19 milligrams to 20milligrams, 20 milligrams to 25 milligrams, 25 milligrams to 30milligrams, 30 milligrams to 35 milligrams, 35 milligrams to 40milligrams, 40 milligrams to 45 milligrams, 45 milligrams to 50milligrams, 50 milligrams to 60 milligrams, 60 milligrams to 70milligrams, 70 milligrams to 80 milligrams, 80 milligrams to 90milligrams, 90 milligrams to 100 milligrams, 100 milligrams to 125milligrams, 125 milligrams to 150 milligrams, 150 milligrams to 175milligrams, 175 milligrams to 200 milligrams, 200 milligrams to 250milligrams, 250 milligrams to 300 milligrams, 300 milligrams to 350milligrams, 350 milligrams to 400 milligrams, 400 milligrams to 450milligrams, or 450 milligrams to 500 milligrams.

In embodiments, each serving size of the foodstuff includes atetrahydrocannabinol content in milligrams per serving ranging from 0milligrams to 0.5 milligrams, 0.5 milligrams to 1 milligrams, 1milligrams to 1.5 milligrams, 1.5 milligrams to 2 milligrams, 2milligrams to 2.5 milligrams, 2.5 milligrams to 3 milligrams, 3milligrams to 3.5 milligrams, 3.5 milligrams to 4 milligrams, 4milligrams to 4.5 milligrams, 4.5 milligrams to 5 milligrams, 5milligrams to 5.5 milligrams, 5.5 milligrams t 6 milligrams, 6milligrams to 6.5 milligrams, 6.5 milligrams to 7 milligrams, 7milligrams to 7.5 milligrams, 7.5 milligrams to 8 milligrams, 8milligrams to 8.5 milligrams, 8.5 milligrams to 9 milligrams, 9milligrams to 9.5 milligrams, 9.5 milligrams to 10 milligrams, 10milligrams to 11 milligrams, 11 milligrams to 12 milligrams, 12milligrams to 13 milligrams, 13 milligrams to 14 milligrams, 14milligrams to 15 milligrams, 15 milligrams to 16 milligrams, 16milligrams to 17 milligrams, 17 milligrams to 18 milligrams, 18milligrams to 19 milligrams, 19 milligrams to 20 milligrams, 20milligrams to 25 milligrams, 25 milligrams to 30 milligrams, 30milligrams to 35 milligrams, 35 milligrams to 40 milligrams, 40milligrams to 45 milligrams, 45 milligrams to 50 milligrams, 50milligrams to 60 milligrams, 60 milligrams to 70 milligrams, 70milligrams to 80 milligrams, 80 milligrams to 90 milligrams, 90milligrams to 100 milligrams, 100 milligrams to 125 milligrams, 125milligrams to 150 milligrams, 150 milligrams to 175 milligrams, 175milligrams to 200 milligrams, 200 milligrams to 250 milligrams, 250milligrams to 300 milligrams, 300 milligrams to 350 milligrams, 350milligrams to 400 milligrams, 400 milligrams to 450 milligrams, or 450milligrams to 500 milligrams.

In embodiments, each serving size of the foodstuff includes apsilocybin, psilocin, baeocystin, and/or norbaeocystin content inmilligrams per serving ranging from 0 milligrams to 0.5 milligrams, 0.5milligrams to 1 milligrams, 1 milligrams to 1.5 milligrams, 1.5milligrams to 2 milligrams, 2 milligrams to 2.5 milligrams, 2.5milligrams to 3 milligrams, 3 milligrams to 3.5 milligrams, 3.5milligrams to 4 milligrams, 4 milligrams to 4.5 milligrams, 4.5milligrams to 5 milligrams, 5 milligrams to 5.5 milligrams, 5.5milligrams t 6 milligrams, 6 milligrams to 6.5 milligrams, 6.5milligrams to 7 milligrams, 7 milligrams to 7.5 milligrams, 7.5milligrams to 8 milligrams, 8 milligrams to 8.5 milligrams, 8.5milligrams to 9 milligrams, 9 milligrams to 9.5 milligrams, 9.5milligrams to 10 milligrams, 10 milligrams to 11 milligrams, 11milligrams to 12 milligrams, 12 milligrams to 13 milligrams, 13milligrams to 14 milligrams, 14 milligrams to 15 milligrams, 15milligrams to 16 milligrams, 16 milligrams to 17 milligrams, 17milligrams to 18 milligrams, 18 milligrams to 19 milligrams, 19milligrams to 20 milligrams, 20 milligrams to 25 milligrams, 25milligrams to 30 milligrams, 30 milligrams to 35 milligrams, 35milligrams to 40 milligrams, 40 milligrams to 45 milligrams, 45milligrams to 50 milligrams, 50 milligrams to 60 milligrams, 60milligrams to 70 milligrams, 70 milligrams to 80 milligrams, 80milligrams to 90 milligrams, 90 milligrams to 100 milligrams, 100milligrams to 125 milligrams, 125 milligrams to 150 milligrams, 150milligrams to 175 milligrams, 175 milligrams to 200 milligrams, 200milligrams to 250 milligrams, 250 milligrams to 300 milligrams, 300milligrams to 350 milligrams, 350 milligrams to 400 milligrams, 400milligrams to 450 milligrams, or 450 milligrams to 500 milligrams, 500milligrams to 1 gram, 1 gram to 2 grams, 2 grams to 3 grams.

In embodiments, the concentrated volatiles (CVOLT*) includepharmaceutical grade purity tetrahydrocannabinol (THC). In embodiments,the concentrated volatiles (CVOLT*) include pharmaceutical grade puritycannabidiol (CBD). In embodiments, the concentrated volatiles (CVOLT*)include pharmaceutical grade purity Δ9-tetrahydrocannabinol Δ9-THC,Δ8-tetrahydrocannabinol Δ8-THC, cannabichromene CBC, cannabidiol CBD,cannabigerol CBG, cannabinidiol CBND, and/or cannabinol CBN. Inembodiments, the concentrated volatiles (CVOLT*) include distilledpharmaceutical grade purity tetrahydrocannabinol (THC). In embodiments,the concentrated volatiles (CVOLT*) include distilled pharmaceuticalgrade purity cannabidiol (CBD). In embodiments, the concentratedvolatiles (CVOLT*) include distilled pharmaceutical grade purityΔ9-tetrahydrocannabinol Δ9-THC, Δ8-tetrahydrocannabinol Δ8-THC,cannabichromene CBC, cannabidiol CBD, cannabigerol CBG, cannabinidiolCBND, and/or cannabinol CBN.

In embodiments, the concentrated volatiles include concentratedvolatiles (CVOLT*). In embodiments, the concentrated volatiles (CVOLT*)includes psilocybin extract, psilocin extract, baeocystin extract,and/or norbaeocystin extract. In embodiments, the concentrated volatiles(CVOLT*) includes psilocybin extract and tetrahydrocannabinol (THC). Inembodiments, the concentrated volatiles (CVOLT*) includes psilocinextract and tetrahydrocannabinol (THC). In embodiments, the concentratedvolatiles (CVOLT*) includes baeocystin extract and tetrahydrocannabinol(THC). In embodiments, the concentrated volatiles (CVOLT*) includesnorbaeocystin extract and tetrahydrocannabinol (THC).

In embodiments, the concentrated volatiles (CVOLT*) includes psilocybinextract and cannabidiol (CBD). In embodiments, the concentratedvolatiles (CVOLT*) includes psilocin extract and cannabidiol (CBD). Inembodiments, the concentrated volatiles (CVOLT*) includes baeocystinextract and cannabidiol (CBD). In embodiments, the concentratedvolatiles (CVOLT*) includes norbaeocystin extract and cannabidiol (CBD).

In embodiments, the concentrated volatiles (CVOLT*) includes psilocybinextract, tetrahydrocannabinol (THC), and cannabidiol (CBD). Inembodiments, the concentrated volatiles (CVOLT*) includes psilocinextract, tetrahydrocannabinol (THC), and cannabidiol (CBD). Inembodiments, the concentrated volatiles (CVOLT*) includes baeocystinextract, tetrahydrocannabinol (THC), and cannabidiol (CBD). Inembodiments, the concentrated volatiles (CVOLT*) includes norbaeocystinextract, tetrahydrocannabinol (THC), and cannabidiol (CBD).

In embodiments, an analyzer (J50*) is configured to analyze at least aportion of the concentrated volatiles (CVOLT*). In embodiments, theanalyzer (J50*) is comprised of one or more analyzers selected from thegroup consisting of Fourier-transform infrared spectroscopy, gaschromatography, high-performance liquid chromatography, liquidchromatograph, liquid chromatography-mass spectrometry, massspectrometry, and ultra-high performance liquid chromatography, andcombinations thereof.

FIG. 17D″

FIG. 17D″ shows a plurality of sequential separation systems (SEPSOL*,SEPSOL**, SEPSOL***) that are configured to separate at least a portionof the solvent, volatiles, and/or cannabinoids from produce concentratedvolatiles (CVOLT*) and a plurality of different compounds (1SCM*,1SCM**, 2SCM*, 2SCM**). Shown in FIG. 17D″ is a first separation system(SEPSOL*) as depicted in FIG. 17D′. The system shows three stages ofseparation, wherein at least one separator is used in each separationstage, the separators include: evaporation, rotary evaporation, vacuumevaporation, distillation, short path distillation, simulated moving bedextraction, chromatography, filtration, adsorption, absorption,molecular distillation, crystallization, vacuum flashing, wiped-filmevaporation, emulsification, filtration, spray drying, or chilledethanol extraction:

(1) a first separation system (SEPSOL*) is configured to separate atleast a portion of the solvent (SOLV2*) and/or volatiles and/orcannabinoids from the volatiles and solvent mixture (SVSM*) to produceconcentrated volatiles (CVOLT*);

(2) a second separation system (SEPSOL**) configured to separatevolatiles and/or cannabinoids from the concentrated volatiles (CVOLT*)to produce a first separated compound (1SCM*) and a second separatedcompound (1SCM**); and

(3) a third separation system (SEPSOL***) configured to separatevolatiles and/or cannabinoids from the first separated compound (1SCM*)and/or the second separated compound (1SCM*) to produce a thirdseparated compound (2SCM*) and a fourth separated compound (2SCM**).

The first separation system (SEPSOL*) is configured to separate at leasta portion of the solvent (SOLV2*) and/or volatiles and/or cannabinoidsfrom the volatiles and solvent mixture (SVSM*) to produce concentratedvolatiles (CVOLT*). Shown in FIG. 17D″ is a second separation system(SEPSOL**) configured to separate volatiles and/or cannabinoids from theconcentrated volatiles (CVOLT*) to produce a first separated compound(1SCM*) and a second separated compound (1SCM**).

In embodiments, the first separated compound (1SCM*) is THC and asolvent. In embodiments, the second separated compound (1SCM*) is CBDand a solvent. In embodiments, the first separated compound (1SCM*) isTHC and terpenes and a solvent. In embodiments, the second separatedcompound (1SCM*) is CBD and terpenes and a solvent. In embodiments, thefirst separated compound (1SCM*) is THC oil. In embodiments, the secondseparated compound (1SCM*) is CBD oil. In embodiments, the firstseparated compound (1SCM*) is THC and/or CBD. In embodiments, the secondseparated compound (1SCM*) is a solvent. In embodiments, the firstseparated compound (1SCM*) is THC and CBD. In embodiments, the secondseparated compound (1SCM*) is a solvent. In embodiments, the firstseparated compound (1SCM*) is THC. In embodiments, the second separatedcompound (1SCM*) is a CBD. In embodiments, the first separated compound(1SCM*) is THC and/or CBD. In embodiments, the second separated compound(1SCM*) is a solvent and terpenes. In embodiments, the first separatedcompound (1SCM*) is THC and/or CBD. In embodiments, the second separatedcompound (1SCM*) includes terpenes.

In embodiments, the first separated compound (1SCM*) is THC and/or CBD.In embodiments, the second separated compound (1SCM*) includes terpenes.In embodiments, the first separated compound (1SCM*) is psilocybinextract. In embodiments, the second separated compound (1SCM*) psilocinextract. In embodiments, the first separated compound (1SCM*) isbaeocystin extract. In embodiments, the second separated compound(1SCM*) norbaeocystin extract. In embodiments, the first separatedcompound (1SCM*) is psilocybin extract and/or psilocin extract. Inembodiments, the second separated compound (1SCM*) baeocystin extractand/or norbaeocystin extract.

In embodiments, a second analyzer (J51*) is configured to analyze atleast a portion of the first separated compound (1SCM*) and/or thesecond separated compound (1SCM*). In embodiments, the analyzer (J50*)is comprised of one or more analyzers selected from the group consistingof Fourier-transform infrared spectroscopy, gas chromatography,high-performance liquid chromatography, liquid chromatograph, liquidchromatography-mass spectrometry, mass spectrometry, and ultra-highperformance liquid chromatography.

Shown in FIG. 17D″ is a third separation system (SEPSOL***) configuredto separate volatiles and/or cannabinoids from the first separatedcompound (1SCM*) and/or the second separated compound (1SCM*) to producea third separated compound (2SCM*) and a fourth separated compound(2SCM**). FIG. 17D″ shows a third separation system (SEPSOL*) configuredto separate cannabinoids into separate isolated substantially pureand/or pure molecular compounds such as TCH and/or CBD. FIG. 17D″ showsa third separation system (SEPSOL*) configured to separate extracts intoseparate isolated molecular compounds such as is psilocybin extract,psilocin extract, baeocystin extract. norbaeocystin extract.

In embodiments, the third separated compound (2SCM*) is terpenes and asolvent. In embodiments, the fourth separated compound (2SCM*) is asolvent. In embodiments, the third separated compound (2SCM*) isterpenes. In embodiments, the fourth separated compound (2SCM*) is asolvent. In embodiments, the third separated compound (2SCM*) is THC anda solvent. In embodiments, the fourth separated compound (2SCM*) is CBDand a solvent. In embodiments, the third separated compound (2SCM*) isTHC and terpenes and a solvent. In embodiments, the fourth separatedcompound (2SCM*) is CBD and terpenes and a solvent. In embodiments, thethird separated compound (2SCM*) is THC oil. In embodiments, the fourthseparated compound (2SCM*) is CBD oil. In embodiments, the thirdseparated compound (2SCM*) is THC and/or CBD. In embodiments, the fourthseparated compound (2SCM*) is a solvent. In embodiments, the thirdseparated compound (2SCM*) is THC and/or CBD. In embodiments, the fourthseparated compound (2SCM*) is a solvent and terpenes. In embodiments,the third separated compound (2SCM*) is THC and/or CBD. In embodiments,the fourth separated compound (2SCM*) includes terpenes. In embodiments,the third separated compound (2SCM*) is THC and/or CBD. In embodiments,the fourth separated compound (2SCM*) includes terpenes. In embodiments,the third separated compound (2SCM*) is psilocybin extract. Inembodiments, the fourth separated compound (2SCM*) psilocin extract. Inembodiments, the third separated compound (2SCM*) is baeocystin extract.In embodiments, the fourth separated compound (2SCM*) norbaeocystinextract.

In embodiments, a third analyzer (J52*) is configured to analyze atleast a portion of the third separated compound (2SCM*) and/or fourthseparated compound (2SCM*). In embodiments, the analyzer (J50*) iscomprised of one or more analyzers selected from the group consisting ofFourier-transform infrared spectroscopy, gas chromatography,high-performance liquid chromatography, liquid chromatograph, liquidchromatography-mass spectrometry, mass spectrometry, and ultra-highperformance liquid chromatography.

In embodiments, both of the first separated compound (1SCM*) and secondseparated compound (1SCM**) are introduced into the third separationsystem (SEPSOL***). In embodiments, only one of the first separatedcompound (1SCM*) or second separated compound (1SCM**) are introducedinto the third separation system (SEPSOL***).

In embodiments, the psilocybin and/or psilocin can be separated from thepsilocybin and/or the psilocin in the first or second stage separator ifany one of the system of separation are used: evaporation, rotaryevaporation, vacuum evaporation, distillation, short path distillation,simulated moving bed extraction, chromatography, filtration, adsorption,absorption, molecular distillation, crystallization, vacuum flashing,wiped-film evaporation, emulsification, filtration, spray drying, orethanol extraction

In embodiments, the baeocystin and norbaeocystin can be separated fromthe psilocybin and/or the psilocin in the second or third stageseparator if any one of the system of separation are used: evaporation,rotary evaporation, vacuum evaporation, distillation, short pathdistillation, simulated moving bed extraction, chromatography,filtration, adsorption, absorption, molecular distillation,crystallization, vacuum flashing, wiped-film evaporation,emulsification, filtration, spray drying, or ethanol extraction.

In embodiments, the crystallizer and/or spray drier may be configured toproduce crystalline psilocybin, psilocin, baeocystin, and/ornorbaeocystin. In embodiments, the crystallizer and/or spray drierseparate a mixture of at least two or more selected from the groupconsisting of psilocybin, psilocin, baeocystin, and/or norbaeocystin. Inembodiments, psilocybin mushrooms are grown, grinded (to a reducedparticle size), and mixed with ethanol for a duration of time selectedfrom the group consisting of 1 second to 5 seconds, 5 seconds to 15seconds, 15 seconds to 30 seconds, 30 seconds to 1 minute, 1 minute to 2minutes, 2 minutes to 3 minutes, 3 minutes to 4 minutes, 4 minutes to 5minutes, 5 minutes to 10 minutes, 10 minutes to 15 minutes, 15 minutesto 20 minutes, 20 minutes to 25 minutes, 25 minutes to 30 minutes, 30minutes to 35 minutes, 35 minutes to 40 minutes, 40 minutes to 45minutes, 45 minutes to 50 minutes, 50 minutes to 55 minutes, 55 minutesto 1 hours, 1 hours to 1.25 hours, 1.25 hours to 1.5 hours, 1.5 hours to1.75 hours, 1.75 hours to 2 hours, 2 hours to 2.5 hours, 2.5 hours to 3hours, 3 hours to 3.5 hours, 3.5 hours to 4 hours, 4 hours to 4.5 hours,4.5 hours to 5 hours, 5 hours to 5.5 hours, 5.5 hours to 6 hours, 7hours to 8 hours, 9 hours to 10 hours, 11 hours to 12 hours, 13 hours to14 hours, 15 hours to 16 hours, 17 hours to 18 hours, 19 hours to 20hours, 21 hours to 22 hours, 23 hours to 24 hours, 25 hours to 26 hours,27 hours to 28 hours, 29 hours to 30 hours, 31 hours to 32 hours, 33hours to 34 hours, 35 hours to 36 hours, 37 hours to 38 hours, 39 hoursto 40 hours, 41 hours to 42 hours, 43 hours to 44 hours, 45 hours to 46hours, 47 hours to 48 hours, 49 hours to 50 hours, 51 hours to 52 hours,53 hours to 54 hours, 55 hours to 56 hours, 57 hours to 58 hours, 59hours to 60 hours, 61 hours to 62 hours, 63 hours to 64 hours, 65 hoursto 66 hours, 67 hours to 68 hours, 69 hours to 70 hours, or 71 hours to72 hours.

In embodiments, the crystallizer has a crystal growth rate ranging from0.05 to 0.1 millimeters per mour (mm/hr), 0.1 to 0.2 mm/hr, 0.2 to 0.3mm/hr, 0.3 to 0.4 mm/hr, 0.4 to 0.5 mm/hr, 0.5 to 0.6 mm/hr, 0.6 to 0.7mm/hr, 0.7 to 0.8 mm/hr, 0.8 to 0.9 mm/hr, 1 to 2 mm/hr, 2 to 3 mm/hr, 3to 4 mm/hr, 4 to 5 mm/hr, 5 to 6 mm/hr, 6 to 7 mm/hr, 7 to 8 mm/hr, or 8to 10 mm/hr. In embodiments, the crystallizer operates at aconcentration to saturated concentration (C/Csat) ratio ranging from1.01 to 1.02, 1.02 to 1.03, 1.03 to 1.04, 1.04 to 1.05, 1.05 to 1.1, 1.1to 1.2, or 1.2 to 1.3.

The ethanol extracts any of the psilocybin, psilocin, baeocystin, and/ornorbaeocystin from the mushrooms to produce a liquid mixture. The liquidmixture than may be filtered to remove the solids including groundmushrooms (at least the caps and stems) to produce a solids depletedliquid mixture, the solids depleted liquid mixture has a reduced amountof solids relative to the liquid mixture. The liquid mixture can be usedto make foodstuff or be mixed with any variety of insect and/or cannabismixtures during any stage of processing disclosed in this patentspecification (shaped insects, cooked insects, flavored insects, insectbeverages, cannabis beverages, cannabis foodstuffs, cannabis and insectfoodstuffs and compositions, etc.).

In embodiments, the solids depleted liquid mixture is then introduced toan evaporation step to reduce the amount of ethanol in the solidsdepleted liquid mixture. The evaporator produces a concentratedvolatiles mixture which has a reduced amount of solvent relative to thesolids depleted liquid mixture. In embodiments the psilocybin, psilocin,baeocystin, norbaeocystin are referred to as volatiles. The evaporatorproduces a concentrated volatiles mixture which has a reduced amount ofsolvent relative to the solids depleted liquid mixture and includes oneor more selected from the group consisting of psilocybin, psilocin,baeocystin, norbaeocystin.

FIG. 17D″ in Volume II shows a three-stage separation system forremoving solvent from volatiles, then two stages of separating volatilesfrom one another including: the second stage separates one volatile fromanother (e.g. psilocybin, psilocin, baeocystin, norbaeocystin from oneanother), and the third stage for separating another (e.g. psilocybin,psilocin, baeocystin, norbaeocystin from one another). In embodiments, asecond and third solvent and evaporation step are performed. Inembodiments, at least one of the mixtures transferred from the second tothe third stage is a liquid and is filtered. In embodiments, both of themixtures transferred from the second to the third stage is a liquid andis filtered. In embodiments, none of the mixtures transferred from thesecond to the third stage is a liquid and is filtered. In embodiments, asecond solvent is required to be added to the mixture of solvent andextract to be cooled and fileted as shown in FIG. 17C′ in Volume II.

FIG. 17E′

FIG. 17E′ shows one non-limiting embodiment of a solvent separationsystem that is configured to evaporator the second solvent from thesecond volatiles and solvent mixture (SVSM) by use of a spray dryer(KAP).

A plurality of separators separate at least a small particulate portion(KCW) and a large particulate portion (KCY) from a volatiles and gasmixture (KBV) that is discharged in the drying chamber (KBG) of a spraydryer (KAP) evaporator (KAO). The spray dryer (KAP) is type ofevaporator (KAO) that evaporates liquid from a second volatiles andsolvent mixture (SVSM). A first separator (KCA), second separator (KCI),and a third separator (KCR) are configured to accept a volatiles and gasmixture (KBV) from the drying chamber (KBG) of a spray dryer (KAP). Inembodiments, the first separator (KCA) is a cyclone or a filter. Inembodiments, the second separator (KCI) is a cyclone or a filter. Inembodiments, the third separator (KCR) is a sifter or a filter. Thethird separator (KCR) accepts first separated volatiles (KCG) from thefirst separator (KCA) and second separated volatiles (KCP) from thesecond separator (KCI) and separates at least a small particulateportion (KCW) and a large particulate portion (KCY) therefrom. Inembodiments, the small particulate portion (KCW) and a large particulateportion (KCY) are crystals, solids, and contain tetrahydrocannabinol(THC).

The second volatiles and solvent mixture (SVSM) is introduced to aliquid input (KAR) of the spray dryer (KAP). The spray dryer (KAP) has atop (K-T) and a bottom (K-B). The spray dryer (KAP) has a vertical axis(KYY) and a horizontal axis (KXY). As shown in FIG. 17E′, the liquidinput (KAR) is located positioned towards the top (K-T) of the spraydryer (KAP). In embodiments, the liquid input (KAR) to the spray dryer(KAP) is positioned closer to the bottom (K-B) of the spray dryer (KAP).

In embodiments, the range of height of the drying chamber (KBG) isselected from one or more from the group 6 feet tall to 8 feet tall, 8feet tall to 10 feet tall, 10 feet tall to 12 feet tall, 12 feet tall to14 feet tall, 14 feet tall to 16 feet tall, 16 feet tall to 18 feettall, 18 feet tall to 20 feet tall, 20 feet tall to 22 feet tall, 22feet tall to 24 feet tall, 24 feet tall to 26 feet tall, 26 feet tall to28 feet tall, 28 feet tall to 30 feet tall, 30 feet tall to 32 feettall, 32 feet tall to 34 feet tall, 34 feet tall to 36 feet tall, 36feet tall to 38 feet tall, 38 feet tall to 40 feet tall, and 40 feettall to 50 feet tall.

In embodiments, the range of diameter of the drying chamber (KBG) isselected from one or more from the group 2 feet in diameter to 4 feet indiameter, 4 feet in diameter to 6 feet in diameter, 6 feet in diameterto 8 feet in diameter, 8 feet in diameter to 10 feet in diameter, 10feet in diameter to 12 feet in diameter, 12 feet in diameter to 14 feetin diameter, 14 feet in diameter to 16 feet in diameter, 16 feet indiameter to 18 feet in diameter, 18 feet in diameter to 20 feet indiameter, 20 feet in diameter to 22 feet in diameter, 22 feet indiameter to 24 feet in diameter, 24 feet in diameter to 26 feet indiameter, 26 feet in diameter to 28 feet in diameter, 28 feet indiameter to 30 feet in diameter, 30 feet in diameter to 32 feet indiameter, 32 feet in diameter to 34 feet in diameter, 34 feet indiameter to 36 feet in diameter, 36 feet in diameter to 38 feet indiameter, and 38 feet in diameter to 40 feet in diameter. Inembodiments, the drying chamber (KBG) is comprised of a material that isselected from one or more from the group consisting of carbon steel,graphite, Hastelloy alloy, nickel, stainless steel, tantalum, andtitanium.

A flow sensor (KEQ) is made available to measure the flow to the secondvolatiles and solvent mixture (SVSM) prior to being introduced to thespray dryer (KAP). The flow sensor (KEQ) is configured to input oroutput a signal (KER) to the computer (COMP). The flow sensor (KEQ)measures the flow of the second volatiles and solvent mixture (SVSM)that is introduced to the liquid input (KAR) of the spray dryer (KAP). Avalve (KEC) is positioned to regulate the flow of the second volatilesand solvent mixture (SVSM) prior to being introduced to the spray dryer(KAP). The valve (KEC) has a controller (KED) that is configured toinput or output a signal (KEE) to the computer (COMP). The valve (KEC)and the flow sensor (KEQ) may be used together in a flow control loop toset the flowrate of spray dryer (KAP) to a flow rate that includes oneor more from the group consisting of: 0.5 gallons per minute (GPM) to 1GPM, 1 GPM to 1.5 GPM, 1.5 GPM to 2 GPM, 2 GPM to 2.5 GPM, 2.5 GPM to 3GPM, 3 GPM to 3.5 GPM, 3.5 GPM to 4 GPM, 4 GPM to 4.5 GPM, 4.5 GPM to 5GPM, 5 GPM to 5.5 GPM, 5.5 GPM to 6 GPM, 6 GPM to 6.5 GPM, 6.5 GPM to 7GPM, 7 GPM to 7.5 GPM, 7.5 GPM to 8 GPM, 8 GPM to 8.5 GPM, 8.5 GPM to 9GPM, 9 GPM to 9.5 GPM, 9.5 GPM to 10 GPM, and 10 GPM to 10.5 GPM.

In embodiments, the second solvent content of the second volatiles andsolvent mixture (SVSM) that is transferred to the mixture input (KAR) ofthe spray dryer (KAP) ranges between 50 weight percent solvent and 95weight percent solvent. In embodiments, the solvent content of thesecond volatiles and solvent mixture (SVSM) that is transferred to themixture input (KAR) of the spray dryer (KAP) ranges between 60 weightpercent solvent and 92 weight percent solvent.

In embodiments, the second volatiles and solvent mixture (SVSM) ispressurized. An inlet pressure sensor (KBE) is provided to measure theinlet pressure prior to the spray dryer (KAP). The inlet pressure sensor(KBE) measures the pressure of the second volatiles and solvent mixture(SVSM) that is introduced to the liquid input (KAR) of the spray dryer(KAP). The inlet pressure sensor (KBE) transmits a signal (KBF) to thecomputer (COMP).

In embodiments, the range of pressure that the inlet pressure sensor(KBE) transmits to the computer (COMP) ranges from one or more from thegroup consisting of: 5 pounds per square inch (PSI) to 10 PSI; 10 PSI to15 PSI; 15 PSI to 20 PSI; 20 PSI to 25 PSI; 25 PSI to 30 PSI; 30 PSI to35 PSI; 35 PSI to 40 PSI; 40 PSI to 45 PSI; 45 PSI to 50 PSI; 50 PSI to55 PSI; 55 PSI to 60 PSI; 60 PSI to 65 PSI; 65 PSI to 70 PSI; 70 PSI to75 PSI; 75 PSI to 80 PSI; 80 PSI to 85 PSI; 85 PSI to 90 PSI; 90 PSI to95 PSI; 95 PSI to 100 PSI; 100 PSI to 125 PSI; 125 PSI to 145 PSI; 145PSI to 170 PSI; 170 PSI to 195 PSI; 195 PSI to 200 PSI; 200 PSI to 220PSI; 220 PSI to 250 PSI; 250 PSI to 275 PSI; 275 PSI to 300 PSI; 300 PSIto 350 PSI; 350 PSI to 402 PSI; 402 PSI to 463 PSI; 463 PSI to 532 PSI;532 PSI to 612 PSI; 612 PSI to 704 PSI; 704 PSI to 809 PSI; 809 PSI to930 PSI; 930 PSI to 1070 PSI; 1,070 PSI to 1,231 PSI; 1,231 PSI to 1,415PSI; 1,415 PSI to 1,627 PSI; 1,627 PSI to 1,872 PSI; 1,872 PSI to 2,152PSI; 2,152 PSI to 2,475 PSI; 2,475 PSI to 2,846 PSI; 2,846 PSI to 3,273PSI; 3,273 PSI to 3,764 PSI; 3,764 PSI to 4,329 PSI; 4,329 PSI to 4,978PSI; 4,978 PSI to 5,725 PSI; 5,725 PSI to 6,584 PSI; 6,584 PSI to 7,571PSI; 7,571 PSI to 8,707 PSI; 8,707 PSI to 10,013 PSI; 10,013 PSI to11,515 PSI; and 11,515 PSI to 15,000 PSI.

In embodiments, the residence time of the second volatiles and solventmixture (SVSM) and gas supply (KAG) within the spray dryer (KAP) ordrying chamber (KBG) ranges from one or more from the group selectedfrom: 0.1 seconds to 1 seconds, 1 seconds to 2 seconds, 2 seconds to 3seconds, 3 seconds to 4 seconds, 4 seconds to 5 seconds, 5 seconds to 6seconds, 6 seconds to 7 seconds, 7 seconds to 8 seconds, 8 seconds to 9seconds, 9 seconds to 10 seconds, 10 seconds to 12 seconds, 12 secondsto 15 seconds, 15 seconds to 20 seconds, 20 seconds to 25 seconds, 25seconds to 30 seconds, 30 seconds to 35 seconds, 35 seconds to 40seconds, 40 seconds to 45 seconds, 45 seconds to 50 seconds, 50 secondsto 55 seconds, 55 seconds to 60 seconds, 60 seconds to 65 seconds, 65seconds to 70 seconds, 70 seconds to 80 seconds, 80 seconds to 90seconds, 90 seconds to 100 seconds, 100 seconds to 110 seconds, and 110seconds to 120 seconds.

A gas supply (KAG) is made available to the spray dryer (KAP) via a gasinput (KAQ). In embodiments, the gas supply (KAG) may include a gas. Inembodiments, the gas supply (KAG) may include a carbon dioxide. Inembodiments, the gas supply (KAG) may include air. In embodiments, thegas supply (KAG) may include an oxygen-containing gas which includesair, oxygen-enriched-air i.e. greater than 21 mole % O2, andsubstantially pure oxygen, i.e. greater than about 95 mole % oxygen (theremainder usually comprising N2 and rare gases). In embodiments, the gassupply (KAG) may include flue gas which includes a vapor or gaseousmixture containing varying amounts of nitrogen (N2), carbon dioxide(CO2), water (H2O), and oxygen (O2). Flue gas is generated from thethermochemical process of combustion. In embodiments, the gas supply(KAG) may include a combustion stream.

A filter (KAH) is made available to remove particulates from the gassupply (KAG) prior to being introduced to the gas input (KAQ) of thespray dryer (KAP). A filter (KAH) may include a sorbent (KAH′) and beconfigured to adsorb and/or absorb at least one component that iscontained within the gas supply (KAG) prior to being introduced to thegas input (KAQ) of the spray dryer (KAP). In embodiments, the filter(KAH) may be a dehumidifier. In embodiments, the filter (KAH) may removewater from the gas supply (KAG) using an adsorbent. In embodiments, theadsorbent used in the filter (KAH) be selected from one or more from thegroup consisting of 3 Angstrom molecular sieve, 3 Angstrom zeolite, 4Angstrom molecular sieve, 4 Angstrom zeolite, activated alumina,activated carbon, adsorbent, alumina, carbon, catalyst, clay, desiccant,molecular sieve, polymer, resin, and silica gel. In embodiments, thefilter (KAH) may include any conceivable means to remove moisture fromthe gas supply (KAG), such as an air conditioner, cooling tower, anadsorber, a plurality of adsorbers. In embodiments, the filter (KAH) mayinclude a cooling tower followed by an adsorber. In embodiments, thefilter (KAH) may include a cooling tower followed by a plurality ofadsorbers. In embodiments, an adsorber is a packed bed of adsorbent. Inembodiments, an adsorber is a moving bed of adsorbent. In embodiments,an adsorber contains an adsorbent.

A fan (KAI) is made available and is configured to introduce the gassupply (KAG) to the spray dryer (KAP). The fan (KAI) is equipped with amotor (KAJ) that has a controller (KAK) which is configured to input oroutput a signal (KAL) to the computer (COMP). In embodiments, the fan(KAI) operates within a range that is selected from one or more from thegroup consisting of: 350 standard cubic feet per minute (SCFM) to 3,500SCFM; 700 SCFM to 7,000 SCFM; 1,050 SCFM to 10,500 SCFM; 1,400 SCFM to14,000 SCFM; 1,750 SCFM to 17,500 SCFM; 2,100 SCFM to 21,000 SCFM; 2,450SCFM to 24,500 SCFM; 2,800 SCFM to 28,000 SCFM; 3,150 SCFM to 31,500SCFM; 3,500 SCFM to 35,000 SCFM; 3,850 SCFM to 38,500 SCFM; 4,200 SCFMto 42,000 SCFM; 4,550 SCFM to 45,500 SCFM; 4,900 SCFM to 49,000 SCFM;5,250 SCFM to 52,500 SCFM; 5,600 SCFM to 56,000 SCFM; 5,950 SCFM to59,500 SCFM; 6,300 SCFM to 63,000 SCFM; 6,650 SCFM to 66,500 SCFM; 7,000SCFM to 70,000 SCFM; and 7,350 SCFM to 73,500 SCFM.

In embodiments, at a second volatiles and solvent mixture (SVSM) flowrate of 0.5 to 1 GPM, the fan (KAI) operates in a range between 350standard cubic feet per minute (SCFM) to 3,500 SCFM. In embodiments, ata second volatiles and solvent mixture (SVSM) flow rate of 0.5 to 1 GPM,the fan (KAI) operates in a range between 700 SCFM to 7,000 SCFM. Inembodiments, at a second volatiles and solvent mixture (SVSM) flow rateof 1 to 1.5 GPM, the fan (KAI) operates in a range between 1,050 SCFM to10,500 SCFM. In embodiments, at a second volatiles and solvent mixture(SVSM) flow rate of 1.5 to 5 GPM, the fan (KAI) operates in a rangebetween 1,400 SCFM to 14,000 SCFM. In embodiments, at a second volatilesand solvent mixture (SVSM) flow rate of 2 to 2.5 GPM, the fan (KAI)operates in a range between 1,750 SCFM to 17,500 SCFM. In embodiments,at a second volatiles and solvent mixture (SVSM) flow rate of 2.5 to 3GPM, the fan (KAI) operates in a range between 2,100 SCFM to 21,000SCFM. In embodiments, at a second volatiles and solvent mixture (SVSM)flow rate of 3 to 3.5 GPM, the fan (KAI) operates in a range between2,450 SCFM to 24,500 SCFM. In embodiments, at a second volatiles andsolvent mixture (SVSM) flow rate of 3.5 to 4 GPM, the fan (KAI) operatesin a range between 2,800 SCFM to 28,000 SCFM. In embodiments, at asecond volatiles and solvent mixture (SVSM) flow rate of 4 to 4.5 GPM,the fan (KAI) operates in a range between 3,150 SCFM to 31,500 SCFM. Inembodiments, at a second volatiles and solvent mixture (SVSM) flow rateof 4.5 to 5 GPM, the fan (KAI) operates in a range between 3,500 SCFM to35,000 SCFM. In embodiments, at a second volatiles and solvent mixture(SVSM) flow rate of 5 to 5.5 GPM, the fan (KAI) operates in a rangebetween 3,850 SCFM to 38,500 SCFM. In embodiments, at a second volatilesand solvent mixture (SVSM) flow rate of 5.5 to 6 GPM, the fan (KAI)operates in a range between 4,200 SCFM to 42,000 SCFM. In embodiments,at a second volatiles and solvent mixture (SVSM) flow rate of 6 to 6.5GPM, the fan (KAI) operates in a range between 4,550 SCFM to 45,500SCFM. In embodiments, at a second volatiles and solvent mixture (SVSM)flow rate of 6.5 to 7 GPM, the fan (KAI) operates in a range between4,900 SCFM to 49,000 SCFM. In embodiments, at a second volatiles andsolvent mixture (SVSM) flow rate of 7 to 7.5 GPM, the fan (KAI) operatesin a range between 5,250 SCFM to 52,500 SCFM. In embodiments, at asecond volatiles and solvent mixture (SVSM) flow rate of 7.5 to 8 GPM,the fan (KAI) operates in a range between 5,600 SCFM to 56,000 SCFM. Inembodiments, at a second volatiles and solvent mixture (SVSM) flow rateof 8 to 8.5 GPM, the fan (KAI) operates in a range between 5,950 SCFM to59,500 SCFM. In embodiments, at a second volatiles and solvent mixture(SVSM) flow rate of 8.5 to 9 GPM, the fan (KAI) operates in a rangebetween 6,300 SCFM to 63,000 SCFM. In embodiments, at a second volatilesand solvent mixture (SVSM) flow rate of 9 to 9.5 GPM, the fan (KAI)operates in a range between 6,650 SCFM to 66,500 SCFM. In embodiments,at a second volatiles and solvent mixture (SVSM) flow rate of 9.5 to 10GPM, the fan (KAI) operates in a range between 7,000 SCFM to 70,000SCFM. In embodiments, at a second volatiles and solvent mixture (SVSM)flow rate of 10 to 10.5 GPM, the fan (KAI) operates in a range between7,350 SCFM to 73,500 SCFM.

An air heater (KAF) is made available to heat the gas supply (KAG) priorto being introduced to the gas input (KAQ) of the spray dryer (KAP).FIG. 17E′ shows the gas supply (KAG) first entering the filter (KAH),then the fan (KAI), and then the air heater (KAF). It is to be notedthat combinations of the filter (KAH), fan (KAI), and air heater (KAF)shown in FIG. 17E′ are non-limiting. For example, the fan (KAI) may bebefore the filter (KAH), the fan (KAI) may be after the air heater(KAF), the filter (KAH) may be after the fan (KAI), the filter (KAH) maybe after the air heater (KAF), the air heater (KAF) may be before thefan (KAI). The air heater (KAF) provides a heated gas supply (KAG) tothe spray dryer (KAP).

In embodiments, the ideal range that the temperature sensor (KAM) inputsinto the computer (COMP) while measuring the heated gas supply (KAG) ispreferably set to 250 degrees Fahrenheit to 600 degrees Fahrenheit, butmore preferably to 300 degrees Fahrenheit to 5000 degrees Fahrenheit,but more preferably to 350 degrees Fahrenheit to 450 degrees Fahrenheit.In embodiments, the heated gas supply (KAG) has a temperature selectedfrom the group consisting of: 250 degrees Fahrenheit to 275 degreesFahrenheit; 275 degrees Fahrenheit to 300 degrees Fahrenheit; 300degrees Fahrenheit to 325 degrees Fahrenheit; 325 degrees Fahrenheit to350 degrees Fahrenheit; 350 degrees Fahrenheit to 375 degreesFahrenheit; 375 degrees Fahrenheit to 400 degrees Fahrenheit; 400degrees Fahrenheit to 425 degrees Fahrenheit; 425 degrees Fahrenheit to450 degrees Fahrenheit; 450 degrees Fahrenheit to 475 degreesFahrenheit; 475 degrees Fahrenheit to 500 degrees Fahrenheit; 500degrees Fahrenheit to 525 degrees Fahrenheit; 525 degrees Fahrenheit to550 degrees Fahrenheit; 550 degrees Fahrenheit to 575 degreesFahrenheit; 575 degrees Fahrenheit to 600 degrees Fahrenheit; 600degrees Fahrenheit to 625 degrees Fahrenheit; 625 degrees Fahrenheit to650 degrees Fahrenheit; 650 degrees Fahrenheit to 675 degreesFahrenheit; 675 degrees Fahrenheit to 700 degrees Fahrenheit; 700degrees Fahrenheit to 725 degrees Fahrenheit; 725 degrees Fahrenheit to750 degrees Fahrenheit; 750 degrees Fahrenheit to 775 degreesFahrenheit; and 775 degrees Fahrenheit to 800 degrees Fahrenheit.

The temperature sensor (KAM) is configured to input a signal (KAN) tothe computer (COMP). The computer (COMP), temperature sensor (KAM), andthe motor (KAJ) of the fan (KAI) may be used together in a temperaturecontrol loop to maintain a constant pre-determined temperature of heatedgas to the spray dryer (KAP).

In embodiments, the heated gas supply (KAG) is created by indirectcontact with steam in the air heater (KAF). In embodiments, the airheater (KAF) may be electrically heated or heated by a combustion steamor flue gas. The heated gas supply (KAG) may also be a combustionstream. In embodiments, the air heater (KAF) accepts a source of steamfrom a steam drum (LBE) as shown on FIG. 17F′. The steam drum (LBE)provides an eighth steam supply (LDM) to the air heater (KAF), asdiscussed below. The eighth steam supply (LDM) may be saturated orsuperheated steam. A steam flow control valve (KAA) is configured toregulate the flow of the steam that passes through the air heater (KAF).The steam flow control valve (KAA) is equipped with a controller (KAB)that sends a signal (KAC) to or from the computer (COMP).

A flow sensor (KAD) is configured to measure the flow of the steam thatpasses through the air heater (KAF). The flow sensor (KAD) sends asignal (KAE) to the computer (COMP). The computer (COMP), steam flowcontrol valve (KAA), and the flow sensor (KAD) may be used in a controlloop to control the flow of steam that is passed through the air heater(KAF). In embodiments, the computer (COMP), steam flow control valve(KAA), flow sensor (KAD), temperature sensor (KAM), and motor (KAJ) ofthe fan (KAI) may be used together in a temperature control loop tomaintain a constant pre-determined temperature of heated gas to thespray dryer (KAP). The steam flow control valve (KAA) may be positionedbefore or after the air heater (KAF). The air heater (KAF) discharges aneighth condensate (LJA) to the condensate tank (LAP) that is shown onFIG. 17F′. A condensate temperature sensor (KK1) is configured tomeasure the temperature of the eighth condensate (LJA) that leaves theair heater (KAF). The condensate temperature sensor (KK1) sends a signal(KK2) to the computer (COMP).

In embodiments, the solvent separation system separates liquid solventfrom the second volatiles and solvent mixture (SVSM) by converting theliquid into a vapor. In embodiments, the solvent separation systemevaporates liquid from within the second volatiles and solvent mixture(SVSM) by use of an evaporator (KAO). A spray dryer (KAP) is a type ofevaporator (KAO).

In embodiments, the spray dryer (KAP) evaporator (KAO) operates at atemperature greater than the boiling point of the liquid solvent withinthe second volatiles and solvent mixture (SVSM) to vaporize the liquidportion of the second volatiles and solvent mixture (SVSM) into a vapor.In embodiments, the spray dryer (KAP) is configured to mix a heated gassupply (KAG′) with a second volatiles and solvent mixture (SVSM) underprecise computer operated automated control to generate a volatiles andgas mixture (KBV).

In embodiments, the spray dryer (KAP) has an interior (KAP′) whichaccepts both the heated gas supply (KAG′) and the second volatiles andsolvent mixture (SVSM). In embodiments, the spray dryer (KAP) has aninterior (KAP′) which accepts both the heated gas supply (KAG′) via thegas input (KAQ) and the second volatiles and solvent mixture (SVSM) viathe liquid input (KAR). In embodiments, the spray dryer (KAP) isequipped with a plurality of spray nozzles (KBC) that dispense thesecond volatiles and solvent mixture (SVSM) within the interior (KAP′)of the spray dryer (KAP).

In embodiments the spray dryer (KAP) has a drying chamber (KBG) whichevaporates liquid within the second volatiles and solvent mixture(SVSM). In embodiments, interior (KBG′) of the drying chamber (KBG) islocated within the interior (KAP′) of the spray dryer (KAP). Inembodiments the spray dryer (KAP) has an air distributor (KAT) that isconfigured to accept the heated gas supply (KAG′) from the gas input(KAQ) and distribute it to the interior (KAP′) of the drying chamber(KBG). In embodiments, the heated gas supply (KAG′) is introduced to theinterior (KAP′) of the spray dryer (KAP) via the air distributor (KAT)using centrifugal momentum.

In embodiments, the second volatiles and solvent mixture (SVSM) isintroduced to the interior (KAP′) of the spray dryer (KAP) via aplurality of spray nozzles (KBC). In embodiments, the second volatilesand solvent mixture (SVSM) is introduced to the interior (KBG′) of thedrying chamber (KBG) via a plurality of spray nozzles (KBC). Inembodiments, the second volatiles and solvent mixture (SVSM) isintroduced to the interior (KAP′) of the spray dryer (KAP) via a rotaryatomizer (KAU) which may have a spray nozzle (KBC) or a plurality ofspray nozzles (KBC). In embodiments, the second volatiles and solventmixture (SVSM) is introduced to the interior (KBG′) of the dryingchamber (KBG) via a rotary atomizer (KAU). In embodiments, the rotaryatomizer (KAU) dispenses second volatiles and solvent mixture (SVSM) orstart-up liquid (KEO) into the interior (KBG′) of the drying chamber(KBG) via an opening (KBD) or a plurality of openings (KBD) or a spraynozzle (KBC) or a plurality of spray nozzles (KBC).

In embodiments the pressure drop across the opening (KBD), plurality ofopenings (KBD), spray nozzle (KBC), or plurality of spray nozzles (KBC)includes one or more from the group consisting of: 5 pounds per squareinch (PSI) to 10 PSI; 10 PSI to 15 PSI; 15 PSI to 20 PSI; 20 PSI to 25PSI; 25 PSI to 30 PSI; 30 PSI to 35 PSI; 35 PSI to 40 PSI; 40 PSI to 45PSI; 45 PSI to 50 PSI; 50 PSI to 55 PSI; 55 PSI to 60 PSI; 60 PSI to 65PSI; 65 PSI to 70 PSI; 70 PSI to 75 PSI; 75 PSI to 80 PSI; 80 PSI to 85PSI; 85 PSI to 90 PSI; 90 PSI to 95 PSI; 95 PSI to 100 PSI; 100 PSI to125 PSI; 125 PSI to 145 PSI; 145 PSI to 170 PSI; 170 PSI to 195 PSI; 195PSI to 200 PSI; 200 PSI to 220 PSI; 220 PSI to 250 PSI; 250 PSI to 275PSI; 275 PSI to 300 PSI; 300 PSI to 350 PSI; 350 PSI to 402 PSI; 402 PSIto 463 PSI; 463 PSI to 532 PSI; 532 PSI to 612 PSI; 612 PSI to 704 PSI;704 PSI to 809 PSI; 809 PSI to 930 PSI; 930 PSI to 1070 PSI; 1,070 PSIto 1,231 PSI; 1,231 PSI to 1,415 PSI; 1,415 PSI to 1,627 PSI; 1,627 PSIto 1,872 PSI; 1,872 PSI to 2,152 PSI; 2,152 PSI to 2,475 PSI; 2,475 PSIto 2,846 PSI; 2,846 PSI to 3,273 PSI; 3,273 PSI to 3,764 PSI; 3,764 PSIto 4,329 PSI; 4,329 PSI to 4,978 PSI; 4,978 PSI to 5,725 PSI; 5,725 PSIto 6,584 PSI; 6,584 PSI to 7,571 PSI; 7,571 PSI to 8,707 PSI; 8,707 PSIto 10,013 PSI; 10,013 PSI to 11,515 PSI; and 11,515 PSI to 15,000 PSI.

The rotary atomizer (KAU) has a motor (KAV) and a controller (KAW) thatis configured to input or output a signal (KAX) to the computer (COMP).In embodiments, the motor (KAV) of the rotary atomizer (KAU) isconnected to a shaft (KBA). In embodiments, the shaft (KBA) is connectedto a disc (KBB). In embodiments, the disc (KBB) has an opening (KBD) ora plurality of openings (KBD) or spray nozzle (KBC) or a plurality ofspray nozzles (KBC) installed on it. In embodiments, the motor (KAV)rotates the shaft (KBA) which in turn rotates the disc (KBB) and thendistributes the second volatiles and solvent mixture (SVSM) or start-upliquid (KEO) to the interior (KAP′) of the spray dryer (KAP) or theinterior (KBG′) of the drying chamber (KBG).

In embodiments, the spray nozzle (KBC) or plurality of spray nozzles(KBC) each have an opening (KBD). In embodiments, the spray nozzle (KBC)or plurality of spray nozzles (KBC) each have a spray aperture (KK4). Inembodiments, the spray nozzle (KBC) or plurality of spray nozzles (KBC)each have an orifice (KK5). In embodiments, the spray nozzle (KBC) orplurality of spray nozzles (KBC) each have an impingement surface (KK6).

In embodiments, at least a portion of the second volatiles and solventmixture (SVSM) or start-up liquid (KEO) contact an impingement surface(KK6) prior to being dispensed to the interior (KAP′) of the spray dryer(KAP) or the interior (KBG′) of the drying chamber (KBG) via a sprayaperture (KK4). In embodiments, at least a portion of the secondvolatiles and solvent mixture (SVSM) or start-up liquid (KEO) passthrough an orifice (KK5) prior to being dispensed to the interior (KAP′)of the spray dryer (KAP) or the interior (KBG′) of the drying chamber(KBG) via a spray aperture (KK4). In embodiments, at least a portion ofthe second volatiles and solvent mixture (SVSM) or start-up liquid (KEO)pass through the spray nozzle (KBC) or plurality of spray nozzles (KBC)and contact an orifice (KK5) prior to being dispensed to the interior(KAP′) of the spray dryer (KAP) or the interior (KBG′) of the dryingchamber (KBG).

In embodiments, the plurality of spray nozzles (KBC) have a spraypattern is a hollow cone, full cone, or a flat spray. In embodiments,the spray pattern includes is that of the whirling type. In embodiments,the whirling type spray nozzle sprays the second volatiles and solventmixture (SVSM) or start-up liquid (KEO) while rotating the liquid (SVSM,KEO) across a portion of the spray nozzle (KBC). A whirling type spraynozzle (KBC) is one that sprays the second volatiles and solvent mixture(SVSM) or start-up liquid (KEO) while rotating the liquid (SVSM, KEO)across a portion of the spray nozzle (KBC) after a pressure drop hastaken place. A whirling type spray nozzle (KBD) is one that sprays thesecond volatiles and solvent mixture (SVSM) or start-up liquid (KEO)while rotating the liquid (SVSM, KEO) across a portion of the spraynozzle after the liquid or slurry has passed through an orifice.

In embodiments, a whirling type spray nozzle (KBD) includes an orifice(KK5) and an impingement surface (KK6): the orifice (KK5) is configuredto accept second volatiles and solvent mixture (SVSM) or start-up liquid(KEO) and drop the pressure from a first higher pressure to a secondlower pressure, the first pressure being greater than the secondpressure; an impingement surface (KK6) that is configured to accept theliquid (SVSM, KEO) at the second pressure at change its direction toimpart rotational or centrifugal momentum.

A whirling type spray nozzle (KBD) is one that sprays a liquid (SVSM,KEO) under cyclone conditions. In embodiments, the spray nozzle (KBD) iscomprised of ceramic, metal, brass, 316 stainless steel, 316L stainlesssteel, stainless steel, polytetrafluoroethylene (PTFE), or plastic, or acomposite material. In embodiments, the spray nozzle (KBC) opening (KBD)ranges from 0.030 inches to 0.30 inches. In embodiments, the spraynozzle (KBC) opening (KBD) ranges from 0.03 inches to 0.16 inches. Inembodiments, the spray nozzle (KBC) orifice (KK5) ranges from 0.030inches to 0.30 inches. In embodiments, the spray nozzle (KBC) orifice(KK5) ranges from 0.03 inches to 0.16 inches.

In embodiments, the spray nozzle (KBC) has an orifice (KK5) and a sprayaperture (KK4). In embodiments, the spray angle of the spray nozzle(KBC) ranges from 15° to 120°. In embodiments, the spray angle of thespray nozzle (KBC) ranges from 30° to 100°. In embodiments, the sprayangle of the spray nozzle (KBC) ranges from 40° to 90°. In embodiments,the spray angle of the spray nozzle (KBC) ranges from 50° to 85°. Inembodiments, the spray angle of the spray nozzle (KBC) ranges from 70°to 75°. In embodiments, the spray angle of the spray nozzle (KBC) rangesfrom 45° to 89°. In embodiments, the spray angle of the spray nozzle(KBC) ranges from 90° to 134°. In embodiments, the spray angle of thespray nozzle (KBC) ranges from 135° to 179°. In embodiments, the sprayangle of the spray nozzle ranges (KBC) from 180° to 360°.

In embodiments, the spray nozzle (KBC) creates solid volatilesparticulates that have a size selected from one or more from the groupconsisting of: 0.01 microns to 0.1 microns, 0.1 microns to 0.5 microns,0.5 microns to 1 microns, 1 microns to 2 microns, 2 microns to 4microns, 4 microns to 8 microns, 8 microns to 10 microns, 10 microns to20 microns, 20 microns to 30 microns, 30 microns to 40 microns, 40microns to 50 microns, 50 microns to 60 microns, 60 microns to 70microns, 70 microns to 80 microns, 80 microns to 90 microns, 90 micronsto 100 microns, and 100 microns to 200 microns.

In embodiments, the spray nozzle (KBC) creates solid volatilesparticulates that have a size selected from one or more from the groupconsisting of: 0.001 microns to 0.002 microns; 0.002 microns to 0.004microns; 0.004 microns to 0.008 microns; 0.008 microns to 0.016 microns;0.016 microns to 0.032 microns; 0.032 microns to 0.064 microns; 0.064microns to 0.122 microns; 0.128 microns to 0.251 microns; 0.256 micronsto 0.512 microns; 0.512 microns to 1.0 microns; 1.0 microns to 1.5microns; 1.5 microns to 2.3 microns; 2.3 microns to 3.5 microns; 3.5microns to 5.2 microns; 5.2 microns to 7.8 microns; 7.8 microns to 12microns; 12 microns to 17 microns; 17 microns to 26 microns; 26 micronsto 39 microns; 39 microns to 59 microns; 59 microns to 89 microns; 89microns to 133 microns; 133 microns to 199 microns; 199 microns to 299microns; 299 microns to 448 microns; 448 microns to 673 microns; 673microns to 1009 microns; 1009 microns to 1513 microns; 1513 microns to2270 microns; 2270 microns to 3405 microns; 3405 microns to 5108microns; and 5108 microns to 7661 microns.

In embodiments, each spray nozzle (KBC) is affixed to the disc (KAB)using one or more connectors selected from the group consisting ofnational pipe thread, British standard pipe thread, and welded. Inembodiments, the spray nozzle (KBC) is connected to the disc (KAB) using0.25 inch national pipe threads, 0.375 inch national pipe threads, 0.50inch national pipe threads, 0.625 inch national pipe threads, 0.75 inchnational pipe threads, 1 inch national pipe threads, 1.25 inch nationalpipe threads, 1.375 inch national pipe threads, 1.625 inch national pipethreads, 1.75 inch national pipe threads, 1.875 inch national pipethreads, or 2 inch national pipe threads. In embodiments, the spraynozzle (KBC) is connected to the disc (KAB) using a fitting thatincludes 0.25 inch pipe threads, 0.375 inch pipe threads, 0.50 inch pipethreads, 0.625 inch pipe threads, 0.75 inch pipe threads, 1 inch pipethreads, 1.25 inch pipe threads, 1.375 inch pipe threads, 1.625 inchpipe threads, 1.75 inch pipe threads, 1.875 inch pipe threads, or 2 inchpipe threads.

In embodiments, the flow through the disc (KAB) is selected from one ormore from the group consisting of 30 gallons per hour to 90 gallons perhour, 90 gallons per hour to 210 gallons per hour, 210 gallons per hourto 330 gallons per hour, 330 gallons per hour to 450 gallons per hour,and 450 gallons per hour to 630 gallons per hour.

In embodiments, the disc (KAB) is has a plurality of spray nozzles(KBC), the plurality of spray nozzles (KBC) is comprised of a quantityof spray nozzles that is selected from one or more from the groupconsisting of 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17,18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35,36, 37, 38, 39, 40, 41, and 42 spray nozzles.

In embodiments, the disc (KAB) is has a plurality of spray nozzles(KBC), the quantity of spray nozzles (KBC) that are installed on thedisc (KAB) is selected from one or more from the group consisting of: 1spray nozzles to 3 spray nozzles, 3 spray nozzles to 6 spray nozzles, 6spray nozzles to 9 spray nozzles, 9 spray nozzles to 12 spray nozzles,12 spray nozzles to 15 spray nozzles, 15 spray nozzles to 18 spraynozzles, 18 spray nozzles to 21 spray nozzles, 21 spray nozzles to 24spray nozzles, 24 spray nozzles to 27 spray nozzles, 27 spray nozzles to30 spray nozzles, 30 spray nozzles to 33 spray nozzles, 33 spray nozzlesto 36 spray nozzles, 36 spray nozzles to 39 spray nozzles, and 39 spraynozzles to 42 spray nozzles.

In embodiments, where 1 spray nozzles are used, the flow through eachspray nozzle in gallons per hour (GPH) ranges from one of more from thegroup consisting of: 30 GPH to 90 GPH, 90 GPH to 210 GPH, 210 GPH to 330GPH, 330 GPH to 450 GPH, and 450 GPH to 630 GPH. In embodiments, where 2spray nozzles are used, the flow through each spray nozzle ranges fromone of more from the group consisting of: 15 GPH to 45 GPH, 45 GPH to105 GPH, 105 GPH to 165 GPH, 165 GPH to 225 GPH, and 225 GPH to 315 GPH.In embodiments, where 3 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 10GPH to 30 GPH 30 GPH to 70 GPH 70 GPH to 110 GPH 110 GPH to 150 GPH, and150 GPH to 210 GPH.

In embodiments, where 4 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8 GPHto 23 GPH, 23 GPH to 53 GPH, 53 GPH to 83 GPH, 83 GPH to 113 GPH, and113 GPH to 158 GPH. In embodiments, where 5 spray nozzles are used, theflow through each spray nozzle ranges from one of more from the groupconsisting of: 6 GPH to 18 GPH, 18 GPH to 42 GPH, 42 GPH to 66 GPH, 66GPH to 90 GPH, and 90 GPH to 126 GPH. In embodiments, where 6 spraynozzles are used, the flow through each spray nozzle ranges from one ofmore from the group consisting of: 15 GPH to 35 GPH, 35 GPH to 55 GPH,55 GPH to 75 GPH, and 75 GPH to 105 GPH.

In embodiments, where 7 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of:12.857 GPH and 30 GPH, 30 GPH and 47.143 GPH, 47.143 GPH and 64.286 GPH,and 64.286 GPH and 90 GPH. In embodiments, where 8 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 11.250 GPH to 26.250 GPH, 26.250 GPH to 41.250GPH, 41.250 GPH to 56.250 GPH, and 56.250 GPH to 78.750 GPH. Inembodiments, where 9 spray nozzles are used, the flow through each spraynozzle ranges from one of more from the group consisting of: 10.000 GPHto 23.333 GPH, 23.333 GPH to 36.667 GPH, 36.667 GPH to 50.000 GPH, and50.000 GPH to 70.000 GPH.

In embodiments, where 10 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 9 GPHto 21 GPH, 21 GPH to 33 GPH, 33 GPH to 45 GPH, and 45 GPH to 63 GPH. Inembodiments, where 11 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8.182GPH to 19.091 GPH, 19.091 GPH to 30.000 GPH, 30.000 GPH to 40.909 GPH,and 40.909 GPH to 57.273 GPH. In embodiments, where 12 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 7.5 GPH to 17.5 GPH, 17.5 GPH to 27.5 GPH, 27.5GPH to 37.5 GPH, and 37.5 GPH to 52.5 GPH.

In embodiments, where 13 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.923GPH to 16.154 GPH, 16.154 GPH to 25.385 GPH, 25.385 GPH to 34.615 GPH,and 34.615 GPH to 48.462 GPH. In embodiments, where 14 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 6.429 GPH to 15.000 GPH, 15.000 GPH to 23.571GPH, 23.571 GPH to 32.143 GPH, and 32.143 GPH to 45.000 GPH. Inembodiments, where 15 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6 GPHto 14 GPH, 14 GPH to 22 GPH, 22 GPH to 30 GPH, and 30 GPH to 42 GPH.

In embodiments, where 16 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of:13.125 GPH to 20.625 GPH, 20.625 GPH to 28.125 GPH, and 28.125 GPH to39.375 GPH. In embodiments, where 17 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 12.353 GPH to 19.412 GPH, 19.412 GPH to 26.471 GPH, and26.471 GPH to 37.059 GPH. In embodiments, where 18 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 11.667 GPH to 18.333 GPH, 18.333 GPH to 25.000GPH, and 25.000 GPH to 35.000 GPH.

In embodiments, where 19 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of:11.053 GPH to 17.368 GPH, 17.368 GPH to 23.684 GPH, and 23.684 GPH to33.158 GPH. In embodiments, where 20 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 10.500 GPH to 16.500 GPH, 16.500 GPH to 22.500 GPH, and22.500 GPH to 31.500 GPH. In embodiments, where 21 spray nozzles areused, the flow through each spray nozzle ranges from one of more fromthe group consisting of: 10.000 GPH to 15.714 GPH, 15.714 GPH to 21.429GPH, and 21.429 GPH to 30.000 GPH.

In embodiments, where 22 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 9.545GPH to 15.000 GPH, 15.000 GPH to 20.455 GPH, and 20.455 GPH to 28.636GPH. In embodiments, where 23 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:9.130 GPH to 14.348 GPH, 14.348 GPH to 19.565 GPH, and 19.565 GPH to27.391 GPH. In embodiments, where 24 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 8.75 GPH to 13.75 GPH, 13.75 GPH to 18.75 GPH, and 18.75GPH to 26.25 GPH.

In embodiments, where 25 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8.40GPH to 13.20 GPH, 13.20 GPH to 18.00 GPH, and 18.00 GPH to 25.20 GPH. Inembodiments, where 26 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 8.077GPH to 12.692 GPH, 12.692 GPH to 17.308 GPH, and 17.308 GPH to 24.231GPH. In embodiments, where 27 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:7.778 GPH to 12.222 GPH, 12.222 GPH to 16.667 GPH, and 16.667 GPH to23.333 GPH.

In embodiments, where 28 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 7.500GPH to 11.786 GPH, 11.786 GPH to 16.071 GPH, and 16.071 GPH to 22.500GPH. In embodiments, where 29 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:7.241 GPH to 11.379 GPH, 11.379 GPH to 15.517 GPH, and 15.517 GPH to21.724 GPH. In embodiments, where 30 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 7 GPH to 11 GPH, 11 GPH to 15 GPH, and 15 GPH to 21 GPH.

In embodiments, where 31 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.774GPH to 10.645 GPH, 10.645 GPH to 14.516 GPH, and 14.516 GPH to 20.323GPH. In embodiments, where 32 spray nozzles are used, the flow througheach spray nozzle ranges from one of more from the group consisting of:

6.563 GPH to 10.313 GPH, 10.313 GPH to 14.063 GPH, and 14.063 GPH to19.688 GPH. In embodiments, where 33 spray nozzles are used, the flowthrough each spray nozzle ranges from one of more from the groupconsisting of: 6.364 GPH to 10.000 GPH, 10.000 GPH to 13.636 GPH, and13.636 GPH to 19.091 GPH.

In embodiments, where 34 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.176GPH to 9.706 GPH, 9.706 GPH to 13.235 GPH, and 13.235 GPH to 18.529 GPH.In embodiments, where 35 spray nozzles are used, the flow through eachspray nozzle ranges from one of more from the group consisting of: 6.000GPH to 9.429 GPH, 9.429 GPH to 12.857 GPH, and 12.857 GPH to 18.000 GPH.In embodiments, where 36 spray nozzles are used, the flow through eachspray nozzle ranges from 9.167 GPH to 12.500 GPH, or 12.500 GPH to17.500 GPH. In embodiments, where 37 spray nozzles are used, the flowthrough each spray nozzle ranges from 8.919 GPH to 12.162 GPH, or 12.162GPH to 17.027 GPH. In embodiments, where 38 spray nozzles are used, theflow through each spray nozzle ranges from 8.684 GPH to 11.842 GPH, or11.842 GPH to 16.579 GPH. In embodiments, where 39 spray nozzles areused, the flow through each spray nozzle ranges from 8.462 GPH to 11.538GPH, or 11.538 GPH to 16.154 GPH. In embodiments, where 40 spray nozzlesare used, the flow through each spray nozzle ranges from 8.250 GPH to11.250 GPH, or 11.250 GPH to 15.750 GPH. In embodiments, where 41 spraynozzles are used, the flow through each spray nozzle ranges 8.049 GPH to10.976 GPH, or 10.976 GPH to 15.366 GPH. In embodiments, where 42 spraynozzles are used, the flow through each spray nozzle ranges from 7.857GPH to 10.714 GPH, or 10.714 GPH to 15.000 GPH.

In embodiments, the drying chamber (KBG) is equipped with a heatingjacket (KBJ), the heating jacket (KBJ) has a heat transfer medium inlet(KBK) and a heat transfer medium outlet (KBL). FIG. 17E′ shows theheating jacket (KBJ) installed over a portion of the drying chamber(KBG) creating an interior (KBJ1) having an annular space within which aheat transfer medium flows. A source of steam is provided to the heattransfer medium inlet (KBK). This steam may be a steam supply (LDP) thatis provided from a steam drum (LBE) as indicated on FIG. 17F′.

In embodiments, a steam trap (KX6) is configured to accept steam,condensate, or non-condensable gases from the interior (KBJ1) of theheating jacket (KBJ) via a heat transfer medium outlet (KBL). Steam,condensate, or non-condensable gases are passed through the valve.During normal operation, only condensate flow through the steam trap(KX6). The condensate the flows through the steam trap (KX6) is theninth condensate (LJB) that is passed to the condensate tank (LAP) asshown on FIG. 17F′.

In embodiments, the steam trap (KX6) is a valve which automaticallydrains the condensate from the interior (KBJ1) of the heating jacket(KBJ) while remaining tight to live steam, or if necessary, allowingsteam to flow at a controlled or adjusted rate. In embodiments, thesteam trap (KX6) also allows non-condensable gases to pass through itwhile remaining tight to steam. In embodiments, the steam trap (KX6) isa mechanical trap such as a bucket trap or a floating ball trap. Inembodiments, the steam trap (KX6) is a thermostatic trap such as abalanced pressure trap or a bimetallic trap. In embodiments, the steamtrap (KX6) is a thermodynamic trap which work by using the difference invelocity between steam and condensate.

In embodiments, a steam flow control valve (KX1) is provided and isconfigured to regulate the flow of steam that is passes through theheating jacket (KBJ). The steam flow control valve (KX1) has acontroller (KX2) which is configured to input or output a signal (KX3)to the computer (COMP). FIG. 17E′ shows the steam flow control valve(KX1) positioned to regulate steam that enters the heat transfer mediuminlet (KBK) of the heating jacket (KBJ). It is to be noted that it isalso contemplated that in certain instances, the steam flow controlvalve (KX1) may be positioned to regulate the heat transfer fluid thatis discharged from the interior (KBJ1) of the heating jacket (KBJ) viathe heat transfer medium outlet (KBL).

In embodiments, a flow sensor (KX4) is provided to measure the flow ofheat transfer fluid that is passes through the heating jacket (KBJ).FIG. 17E′ shows the flow sensor (KX4) positioned to measure the flow ofsteam that enters the heat transfer medium inlet (KBK) of the heatingjacket (KBJ). It is to be noted that it is also contemplated that incertain instances, the flow sensor (KX4) may be positioned to measurethe heat transfer fluid (steam or steam condensate) that is dischargedfrom the interior (KBJ1) of the heating jacket (KBJ) via the heattransfer medium outlet (KBL). The flow sensor (KX4) inputs a signal(KX5) to the computer (COMP).

In embodiment, the heating jacket (KBJ) is configured to maintain thewall (KWG) within the interior (KBG′) drying chamber (KBG) at a constanttemperature. In embodiments, the wall temperature ranges from one ormore from the group consisting of between: 110 degrees Fahrenheit to 125degrees Fahrenheit; 125 degrees Fahrenheit to 140 degrees Fahrenheit;140 degrees Fahrenheit to 155 degrees Fahrenheit; 155 degrees Fahrenheitto 170 degrees Fahrenheit; 170 degrees Fahrenheit to 185 degreesFahrenheit; 185 degrees Fahrenheit to 200 degrees Fahrenheit; 200degrees Fahrenheit to 215 degrees Fahrenheit; 215 degrees Fahrenheit to230 degrees Fahrenheit; 230 degrees Fahrenheit to 245 degreesFahrenheit; 250 degrees Fahrenheit to 275 degrees Fahrenheit; 275degrees Fahrenheit to 300 degrees Fahrenheit; 300 degrees Fahrenheit to325 degrees Fahrenheit; 325 degrees Fahrenheit to 350 degreesFahrenheit; 350 degrees Fahrenheit to 375 degrees Fahrenheit; 375degrees Fahrenheit to 400 degrees Fahrenheit; 400 degrees Fahrenheit to425 degrees Fahrenheit; 425 degrees Fahrenheit to 450 degreesFahrenheit; 450 degrees Fahrenheit to 475 degrees Fahrenheit; 475degrees Fahrenheit to 500 degrees Fahrenheit; 500 degrees Fahrenheit to525 degrees Fahrenheit; 525 degrees Fahrenheit to 550 degreesFahrenheit; 550 degrees Fahrenheit to 575 degrees Fahrenheit; 575degrees Fahrenheit to 600 degrees Fahrenheit; 600 degrees Fahrenheit to625 degrees Fahrenheit; 625 degrees Fahrenheit to 650 degreesFahrenheit; 650 degrees Fahrenheit to 675 degrees Fahrenheit; 675degrees Fahrenheit to 700 degrees Fahrenheit; 700 degrees Fahrenheit to725 degrees Fahrenheit; 725 degrees Fahrenheit to 750 degreesFahrenheit; 750 degrees Fahrenheit to 775 degrees Fahrenheit; and 775degrees Fahrenheit to 800 degrees Fahrenheit.

In embodiments, it is desired to operate the heating jacket (KBJ) tomaintain a wall (KWG) temperature sufficient to avoid sticking,deposition, burning of volatile particulates or liquid upon surface ofthe wall (KWG). In embodiments, the surface of the wall (KWG) transfersheat into the interior (KBG) of the drying chamber (KBG). Inembodiments, it is desired to operate the heating jacket (KBJ) in amanner that is sufficient to maintain a wall (KWG) temperature that isknown to now fouling of the heat surface by sticking, deposition,burning of volatile particulates or liquid upon surface of the wall(KWG). Powder build-up on the wall (KWG) within the interior (KBG′)surface of the drying chamber (KBG) poses problems related to start-upand shutdown as discussed below.

In embodiments, the openings (KM4) of the screen (KM3) or mesh (KM3′)are selected from one or more from the group consisting of 0.01 micronsto 0.1 microns, 0.1 microns to 0.5 microns, 0.5 microns to 1 microns, 1microns to 2 microns, 2 microns to 4 microns, 4 microns to 8 microns, 8microns to 10 microns, 10 microns to 20 microns, 20 microns to 30microns, 30 microns to 40 microns, 40 microns to 50 microns, 50 micronsto 60 microns, 60 microns to 70 microns, 70 microns to 80 microns, 80microns to 90 microns, 90 microns to 100 microns, and 100 microns to 200microns.

In embodiments, the temperature sensor (KBY) positioned on the firsttransfer conduit (KBW) in between the second output (KBU) of the spraydryer (KAP) and the first input (KCB) of the first separator (KCA) thatmeasures the temperature of the volatiles and gas mixture (KBV) ispreferably optimized to be maintained at 120 degrees Fahrenheit to 400degrees Fahrenheit, or between 135 degrees Fahrenheit to 300 degreesFahrenheit, or between 140 degrees Fahrenheit to 160 degrees Fahrenheit,or between 146 degrees Fahrenheit to 154 degrees Fahrenheit. Thetemperature sensor (KBY) inputs a signal (KBX) to the computer (COMP).

In embodiments, the temperature sensor (KBY) positioned on the firsttransfer conduit (KBW) in between the second output (KBU) of the spraydryer (KAP) and the first input (KCB) of the first separator (KCA) thatmeasures the temperature of the volatiles and gas mixture (KBV) ispreferably optimized to be maintained at 150 degrees Fahrenheit to 250degrees Fahrenheit, but more preferably to 135 degrees Fahrenheit to 180degrees Fahrenheit, but more preferably to 145 degrees Fahrenheit to 155degrees Fahrenheit.

In embodiments, the temperature of the volatiles and gas mixture (KBV)leaving the drying chamber (KBG) ranges from one or more from the groupconsisting of between: 110 degrees Fahrenheit to 125 degrees Fahrenheit;125 degrees Fahrenheit to 140 degrees Fahrenheit; 140 degrees Fahrenheitto 155 degrees Fahrenheit; 155 degrees Fahrenheit to 170 degreesFahrenheit; 170 degrees Fahrenheit to 185 degrees Fahrenheit; 185degrees Fahrenheit to 200 degrees Fahrenheit; 200 degrees Fahrenheit to215 degrees Fahrenheit; 215 degrees Fahrenheit to 230 degreesFahrenheit; 230 degrees Fahrenheit to 245 degrees Fahrenheit; 250degrees Fahrenheit to 275 degrees Fahrenheit; 275 degrees Fahrenheit to300 degrees Fahrenheit; 300 degrees Fahrenheit to 325 degreesFahrenheit; 325 degrees Fahrenheit to 350 degrees Fahrenheit; 350degrees Fahrenheit to 375 degrees Fahrenheit; and 375 degrees Fahrenheitto 400 degrees Fahrenheit.

In embodiments, the difference in temperature between the heated gassupply (KAG′) and the volatiles and gas mixture (KBV) ranges frombetween 110 degrees Fahrenheit to 125 degrees Fahrenheit; 125 degreesFahrenheit to 140 degrees Fahrenheit; 140 degrees Fahrenheit to 155degrees Fahrenheit; 155 degrees Fahrenheit to 170 degrees Fahrenheit;170 degrees Fahrenheit to 185 degrees Fahrenheit; 185 degrees Fahrenheitto 200 degrees Fahrenheit; 200 degrees Fahrenheit to 215 degreesFahrenheit; 215 degrees Fahrenheit to 230 degrees Fahrenheit; 230degrees Fahrenheit to 245 degrees Fahrenheit; 250 degrees Fahrenheit to275 degrees Fahrenheit; 275 degrees Fahrenheit to 300 degreesFahrenheit; 300 degrees Fahrenheit to 325 degrees Fahrenheit; 325degrees Fahrenheit to 350 degrees Fahrenheit; 350 degrees Fahrenheit to375 degrees Fahrenheit; 375 degrees Fahrenheit to 400 degreesFahrenheit; 400 degrees Fahrenheit to 425 degrees Fahrenheit; 425degrees Fahrenheit to 450 degrees Fahrenheit; 450 degrees Fahrenheit to475 degrees Fahrenheit; 475 degrees Fahrenheit to 500 degreesFahrenheit.

In embodiments, a pressure sensor (KBH) is configured to measure thepressure within the interior (KBG′) of the drying chamber (KBG) andoutput a signal (KBI) to the computer (COMP). In embodiments, the rangesof pressure within the interior (KBG′) of the drying chamber (KBG) isselected from one of more from the group consisting of: 1.5 pounds persquare inch absolute (PSIA) 3 PSIA, 3 PSIA to 4.5 PSIA, 4.5 PSIA to 6PSIA, 6 PSIA to 7.5 PSIA, 7.5 PSIA to 9 PSIA, 9 PSIA to 10.5 PSIA, 10.5PSIA to 12 PSIA, 12 PSIA to 13.5 PSIA, 12 PSIA to 12.25 PSIA, 12.25 PSIAto 12.5 PSIA, 12.5 PSIA to 12.75 PSIA, 12.75 PSIA to 13 PSIA, 13 PSIA to13.25 PSIA, 13.25 PSIA to 13.5 PSIA, 13.5 PSIA to 13.75 PSIA, 13.75 PSIAto 14 PSIA, 14 PSIA to 14.25 PSIA, 14.25 PSIA to 14.5 PSIA, 14.5 PSIA to14.75 PSIA, 14.75 PSIA to 15 PSIA, 15 PSIA to 16.5 PSIA, 16.5 PSIA to 18PSIA, 18 PSIA to 19.5 PSIA, 19.5 PSIA to 21 PSIA, 21 PSIA to 22.5 PSIA,22.5 PSIA to 24 PSIA, 24 PSIA to 25.5 PSIA, 25.5 PSIA to 27 PSIA, 27PSIA to 28.5 PSIA, 28.5 PSIA to 30 PSIA, 30 PSIA to 31.5 PSIA, 31.5 PSIAto 33 PSIA, 33 PSIA to 34.5 PSIA, and 34.5 PSIA to 36 PSIA.

In embodiments, the ranges of pressure within the interior (KBG′) of thedrying chamber (KBG) is selected from one of more from the groupconsisting of: between about 0.001 inches of water to about 0.002 inchesof water; between about 0.002 inches of water to about 0.003 inches ofwater; between about 0.003 inches of water to about 0.006 inches ofwater; between about 0.006 inches of water to about 0.012 inches ofwater; between about 0.012 inches of water to about 0.024 inches ofwater; between about 0.024 inches of water to about 0.050 inches ofwater; between about 0.050 inches of water to about 0.075 inches ofwater; between about 0.075 inches of water to about 0.150 inches ofwater; between about 0.150 inches of water to about 0.300 inches ofwater; between about 0.300 inches of water to about 0.450 inches ofwater; between about 0.450 inches of water to about 0.473 inches ofwater; between about 0.473 inches of water to about 0.496 inches ofwater; between about 0.496 inches of water to about 0.521 inches ofwater; between about 0.521 inches of water to about 0.547 inches ofwater; between about 0.547 inches of water to about 0.574 inches ofwater; between about 0.574 inches of water to about 0.603 inches ofwater; between about 0.603 inches of water to about 0.633 inches ofwater; between about 0.633 inches of water to about 0.665 inches ofwater; between about 0.665 inches of water to about 0.698 inches ofwater; between about 0.698 inches of water to about 0.733 inches ofwater; between about 0.733 inches of water to about 0.770 inches ofwater; between about 0.770 inches of water to about 0.808 inches ofwater; between about 0.808 inches of water to about 0.849 inches ofwater; between about 0.849 inches of water to about 0.891 inches ofwater; between about 0.891 inches of water to about 0.936 inches ofwater; between about 0.936 inches of water to about 0.982 inches ofwater; between about 0.982 inches of water to about 1.031 inches ofwater; between about 1.031 inches of water to about 1.083 inches ofwater; between about 1.083 inches of water to about 1.137 inches ofwater; between about 1.137 inches of water to about 1.194 inches ofwater; between about 1.194 inches of water to about 1.254 inches ofwater; between about 1.254 inches of water to about 1.316 inches ofwater; between about 1.316 inches of water to about 1.382 inches ofwater; between about 1.382 inches of water to about 1.451 inches ofwater; between about 1.451 inches of water to about 1.524 inches ofwater; between about 1.524 inches of water to about 2.286 inches ofwater; between about 2.286 inches of water to about 3.429 inches ofwater; between about 3.429 inches of water to about 5.143 inches ofwater; between about 5.143 inches of water to about 7.715 inches ofwater; between about 7.715 inches of water to about 11.572 inches ofwater; between about 11.572 inches of water to about 17.358 inches ofwater; between about 17.358 inches of water to about 26.037 inches ofwater; between about 26.037 inches of water to about 39.055 inches ofwater; between about 39.055 inches of water to about 58.582 inches ofwater; between about 58.582 inches of water to about 87.873 inches ofwater; between about 87.873 inches of water to about 131.810 inches ofwater; between about 131.810 inches of water to about 197.715 inches ofwater; between about 197.715 inches of water to about 296.573 inches ofwater; or, between about 296.573 inches of water to about 400 inches ofwater.

Spray dried volatiles (KBT) may be removed from the first output (KB S)of the drying chamber (KBG). In embodiments, the volatiles (KBT) removedfrom the first output (KBS) of the drying chamber (KBG) may be solid ormay contain liquid. In embodiments, the volatiles (KBT) removed from thefirst output (KB S) of the drying chamber (KBG) are either too wet ortoo large, or both, to be evacuated from the second output (KBU) of thedrying chamber (KBG). In embodiments, the volatiles (KBT) removed fromthe first output (KB S) may be mixed with one or more stream ofseparated volatiles, such first separated volatiles (KCG), secondseparated volatiles (KCP), third separated volatiles (KCV), a fourthseparated volatiles (KCX), or a large particulate portion (KCY) to formcombined volatiles (KM7) as shown in FIG. 17E′.

In embodiments, a vibrator (KBN) is connected to the spray dryer (KAP)or drying chamber (KBG) via a connection (KBR). In embodiments, thespray dryer (KAP) or drying chamber (KBG) is equipped with a vibrator(KBN). In embodiments, a vibrator (KBN) vibrates at least a portion ofthe spray dryer (KAP) or drying chamber (KBG) to aide in removal of thespray dried volatiles (KBT) from the first output (KBS). In embodiments,the vibrator (KBN) is pneumatic. In embodiments, the vibrator (KBN)operates at a vibration range that is selected from one or more from thegroup consisting of 3,000 vibrations per minute (VPM) to 4000 VPM, 4,000VPM to 5,000 VPM, 5,000 VPM to 5,500 VPM, 5,500 VPM to 6,000 VPM, 6,000VPM to 6,500 VPM, 6,500 VPM to 7,000 VPM, 7,000 VPM to 7,500 VPM, 7,500VPM to 8,000 VPM, 8,000 VPM to 8,500 VPM, 8,500 VPM to 9,000 VPM, 9,000VPM to 9,500 VPM, 9,500 VPM to 10,000 VPM, 10,000 VPM to 15,000 VPM,15,000 VPM to 20,000 VPM, 20,000 VPM to 25,000 VPM, 25,000 VPM to 30,000VPM, 30,000 VPM to 35,000 VPM, 35,000 VPM to 40,000 VPM, 40,000 VPM to45,000 VPM, and 45,000 VPM to 50,000 VPM. In embodiments, the vibrator(KBN) has a motor (KBO) with a controller (KBP) that is configured toinput or output a signal (KBQ) to the computer (COMP).

In embodiments, the small particulate portion (KCW) has a liquid contentthat ranges from one or more from the group selected from 0.05 weightpercent of liquid to 0.1 weight percent of liquid, 0.1 weight percent ofliquid to 0.2 weight percent of liquid, 0.2 weight percent of liquid to0.4 weight percent of liquid, 0.4 weight percent of liquid to 0.8 weightpercent of liquid, 0.8 weight percent of liquid to 1 weight percent ofliquid, 1 weight percent of liquid to 2 weight percent of liquid, 2weight percent of liquid to 3 weight percent of liquid, 3 weight percentof liquid to 4 weight percent of liquid, 4 weight percent of liquid to 5weight percent of liquid, 5 weight percent of liquid to 6 weight percentof liquid, 6 weight percent of liquid to 7 weight percent of liquid, 7weight percent of liquid to 8 weight percent of liquid, 8 weight percentof liquid to 9 weight percent of liquid, 9 weight percent of liquid to10 weight percent of liquid, 10 weight percent of liquid to 11 weightpercent of liquid, 11 weight percent of liquid to 12 weight percent ofliquid, 12 weight percent of liquid to 13 weight percent of liquid, 13weight percent of liquid to 14 weight percent of liquid, 14 weightpercent of liquid to 15 weight percent of liquid, 15 weight percent ofliquid to 16 weight percent of liquid, 16 weight percent of liquid to 17weight percent of liquid, 17 weight percent of liquid to 18 weightpercent of liquid, 18 weight percent of liquid to 19 weight percent ofliquid, and 19 weight percent of liquid to 20 weight percent of liquid.

In embodiments, the small particulate portion (KCW) has a liquid contentthat ranges from one or more from the group selected from 0.05 weightpercent of liquid to 0.1 weight percent of liquid, 0.1 weight percent ofliquid to 0.2 weight percent of liquid, 0.2 weight percent of liquid to0.4 weight percent of liquid, 0.4 weight percent of liquid to 0.8 weightpercent of liquid, 0.8 weight percent of liquid to 1 weight percent ofliquid, 1 weight percent of liquid to 2 weight percent of liquid, 2weight percent of liquid to 3 weight percent of liquid, 3 weight percentof liquid to 4 weight percent of liquid, 4 weight percent of liquid to 5weight percent of liquid, 5 weight percent of liquid to 6 weight percentof liquid, 6 weight percent of liquid to 7 weight percent of liquid, 7weight percent of liquid to 8 weight percent of liquid, 8 weight percentof liquid to 9 weight percent of liquid, 9 weight percent of liquid to10 weight percent of liquid, 10 weight percent of liquid to 11 weightpercent of liquid, 11 weight percent of liquid to 12 weight percent ofliquid, 12 weight percent of liquid to 13 weight percent of liquid, 13weight percent of liquid to 14 weight percent of liquid, 14 weightpercent of liquid to 15 weight percent of liquid, 15 weight percent ofliquid to 16 weight percent of liquid, 16 weight percent of liquid to 17weight percent of liquid, 17 weight percent of liquid to 18 weightpercent of liquid, 18 weight percent of liquid to 19 weight percent ofliquid, and 19 weight percent of liquid to 20 weight percent of liquid.

In embodiments, the large particulate portion (KCY) has a liquid contentthat ranges from one or more from the group selected from 0.05 weightpercent of liquid to 0.1 weight percent of liquid, 0.1 weight percent ofliquid to 0.2 weight percent of liquid, 0.2 weight percent of liquid to0.4 weight percent of liquid, 0.4 weight percent of liquid to 0.8 weightpercent of liquid, 0.8 weight percent of liquid to 1 weight percent ofliquid, 1 weight percent of liquid to 2 weight percent of liquid, 2weight percent of liquid to 3 weight percent of liquid, 3 weight percentof liquid to 4 weight percent of liquid, 4 weight percent of liquid to 5weight percent of liquid, 5 weight percent of liquid to 6 weight percentof liquid, 6 weight percent of liquid to 7 weight percent of liquid, 7weight percent of liquid to 8 weight percent of liquid, 8 weight percentof liquid to 9 weight percent of liquid, 9 weight percent of liquid to10 weight percent of liquid, 10 weight percent of liquid to 11 weightpercent of liquid, 11 weight percent of liquid to 12 weight percent ofliquid, 12 weight percent of liquid to 13 weight percent of liquid, 13weight percent of liquid to 14 weight percent of liquid, 14 weightpercent of liquid to 15 weight percent of liquid, 15 weight percent ofliquid to 16 weight percent of liquid, 16 weight percent of liquid to 17weight percent of liquid, 17 weight percent of liquid to 18 weightpercent of liquid, 18 weight percent of liquid to 19 weight percent ofliquid, and 19 weight percent of liquid to 20 weight percent of liquid.

In embodiments, the large particulate portion (KCY) has a liquid contentthat ranges from one or more from the group selected from 0.05 weightpercent of liquid to 0.1 weight percent of liquid, 0.1 weight percent ofliquid to 0.2 weight percent of liquid, 0.2 weight percent of liquid to0.4 weight percent of liquid, 0.4 weight percent of liquid to 0.8 weightpercent of liquid, 0.8 weight percent of liquid to 1 weight percent ofliquid, 1 weight percent of liquid to 2 weight percent of liquid, 2weight percent of liquid to 3 weight percent of liquid, 3 weight percentof liquid to 4 weight percent of liquid, 4 weight percent of liquid to 5weight percent of liquid, 5 weight percent of liquid to 6 weight percentof liquid, 6 weight percent of liquid to 7 weight percent of liquid, 7weight percent of liquid to 8 weight percent of liquid, 8 weight percentof liquid to 9 weight percent of liquid, 9 weight percent of liquid to10 weight percent of liquid, 10 weight percent of liquid to 11 weightpercent of liquid, 11 weight percent of liquid to 12 weight percent ofliquid, 12 weight percent of liquid to 13 weight percent of liquid, 13weight percent of liquid to 14 weight percent of liquid, 14 weightpercent of liquid to 15 weight percent of liquid, 15 weight percent ofliquid to 16 weight percent of liquid, 16 weight percent of liquid to 17weight percent of liquid, 17 weight percent of liquid to 18 weightpercent of liquid, 18 weight percent of liquid to 19 weight percent ofliquid, and 19 weight percent of liquid to 20 weight percent of liquid.

In embodiments, the volatiles (KBT) removed the drying chamber (KBG)have a liquid content that ranges from one or more from the groupselected from 0.05 weight percent of liquid to 0.1 weight percent ofliquid, 0.1 weight percent of liquid to 0.2 weight percent of liquid,0.2 weight percent of liquid to 0.4 weight percent of liquid, 0.4 weightpercent of liquid to 0.8 weight percent of liquid, 0.8 weight percent ofliquid to 1 weight percent of liquid, 1 weight percent of liquid to 2weight percent of liquid, 2 weight percent of liquid to 3 weight percentof liquid, 3 weight percent of liquid to 4 weight percent of liquid, 4weight percent of liquid to 5 weight percent of liquid, 5 weight percentof liquid to 6 weight percent of liquid, 6 weight percent of liquid to 7weight percent of liquid, 7 weight percent of liquid to 8 weight percentof liquid, 8 weight percent of liquid to 9 weight percent of liquid, 9weight percent of liquid to 10 weight percent of liquid, 10 weightpercent of liquid to 11 weight percent of liquid, 11 weight percent ofliquid to 12 weight percent of liquid, 12 weight percent of liquid to 13weight percent of liquid, 13 weight percent of liquid to 14 weightpercent of liquid, 14 weight percent of liquid to 15 weight percent ofliquid, 15 weight percent of liquid to 16 weight percent of liquid, 16weight percent of liquid to 17 weight percent of liquid, 17 weightpercent of liquid to 18 weight percent of liquid, 18 weight percent ofliquid to 19 weight percent of liquid, and 19 weight percent of liquidto 20 weight percent of liquid.

In embodiments, the volatiles (KBT) removed the drying chamber (KBG)have a liquid content that ranges from one or more from the groupselected from 0.05 weight percent of liquid to 0.1 weight percent ofliquid, 0.1 weight percent of liquid to 0.2 weight percent of liquid,0.2 weight percent of liquid to 0.4 weight percent of liquid, 0.4 weightpercent of liquid to 0.8 weight percent of liquid, 0.8 weight percent ofliquid to 1 weight percent of liquid, 1 weight percent of liquid to 2weight percent of liquid, 2 weight percent of liquid to 3 weight percentof liquid, 3 weight percent of liquid to 4 weight percent of liquid, 4weight percent of liquid to 5 weight percent of liquid, 5 weight percentof liquid to 6 weight percent of liquid, 6 weight percent of liquid to 7weight percent of liquid, 7 weight percent of liquid to 8 weight percentof liquid, 8 weight percent of liquid to 9 weight percent of liquid, 9weight percent of liquid to 10 weight percent of liquid, 10 weightpercent of liquid to 11 weight percent of liquid, 11 weight percent ofliquid to 12 weight percent of liquid, 12 weight percent of liquid to 13weight percent of liquid, 13 weight percent of liquid to 14 weightpercent of liquid, 14 weight percent of liquid to 15 weight percent ofliquid, 15 weight percent of liquid to 16 weight percent of liquid, 16weight percent of liquid to 17 weight percent of liquid, 17 weightpercent of liquid to 18 weight percent of liquid, 18 weight percent ofliquid to 19 weight percent of liquid, and 19 weight percent of liquidto 20 weight percent of liquid.

In embodiments, the spray dryer (KAP) drying chamber (KBG) is configuredto mix the heated gas supply (KAG′) with the second volatiles andsolvent mixture (SVSM) to form a volatiles and gas mixture (KBV). Thevolatiles and gas mixture (KBV) is discharged from the spray dryer (KAP)via a second output (KBU). The volatiles and gas mixture (KBV) include aspray dried volatiles portion (KBV′), a vapor portion (KBV″), and a gasportion (KBV′″). In embodiments, the spray dried volatiles portion(KBV′) may include solid particulates. In embodiments, the vapor portion(KBV″) is the second solvent. In embodiments, the vapor portion (KBV″)may include the vapor-phase of the liquid within the second volatilesand solvent mixture (SVSM) which may include the second solvent. Inembodiments, the gas portion (KBV″) includes whatever was within the gassupply (KAG).

The spray dryer (KAP) has a second output (KBU) that is configured todischarge a volatiles and gas mixture (KBV) from the interior (KBG′) ofthe drying chamber (KBG). In embodiments, the volatiles and gas mixture(KBV) has a spray dried volatiles portion (KBV′), vapor portion (KBV″),and a gas portion (KBV′″). The second output (KBU) of the spray dryer(KAP) is connected to the first-first input (KCB) of the first separator(KCA) via a first transfer conduit (KBW). In embodiments, the firstseparator (KCA) is a cyclone or a filter. FIG. 17E′ shows the firstseparator (KCA) as a cyclone.

The first transfer conduit (KBW) transfers the volatiles and gas mixture(KBV) from the interior (KBG′) of the drying chamber (KBG) to the firstseparator (KCA). The first separator (KCA) separates first separatedvolatiles (KCG) from the volatiles and gas mixture (KBV) to create afirst volatiles depleted gas stream (KCD). The first volatiles depletedgas stream (KCD) is discharged from the first separator (KCA) via afirst-first output (KCC).

The first separator (KCA) has: a first-first input (KCB) for receivingthe volatiles and gas mixture (KBV) from the spray dryer (KAP), afirst-first output (KCC) for evacuating the first volatiles depleted gasstream (KCD) towards the second separator (KCI), and a first-secondoutput (KCF) for transferring first separated volatiles (KCG) towardsthe third separator (KCR). The first volatiles depleted gas stream (KCD)is transferred from the first-first output (KCC) to the second-firstinput (KCK) of the second separator (KCI) via a second transfer conduit(KCE).

The first volatiles depleted gas stream (KCD) has a reduced amount ofvolatiles relative to the volatiles and gas mixture (KBV). The firstvolatiles depleted gas stream (KCD) has a reduced amount of spray driedvolatiles portion (KBV′) relative to the volatiles and gas mixture(KBV). The second transfer conduit (KCE) is connected at one end to thefirst-first output (KCC) of the first separator (KCA) and at another endto the second-first input (KCK) of the second separator (KCI).

The first separated volatiles (KCG) that are separated from thevolatiles and gas mixture (KBV) are discharged from the first separator(KCA) via the first-second output (KCF). The third-first input (KCS) ofthe third separator (KCR) is configured to receive the first separatedvolatiles (KCG) via a first dipleg (KCH). The first dipleg (KCH) isconnected at one end to the first-second output (KCF) of the firstseparator (KCA) and at a second end to the third-first input (KCS) ofthe third separator (KCR). The first separated volatiles (KCG) includesat least a portion of the spray dried volatiles portion (KBV′) that wereseparated from the volatiles and gas mixture (KBV).

The second separator (KCI) separates second separated volatiles (KCP)from the first volatiles depleted gas stream (KCD) to create a secondvolatiles depleted gas stream (KCM). The second volatiles depleted gasstream (KCM) has a reduced amount of volatiles relative to the firstvolatiles depleted gas stream (KCD). The second volatiles depleted gasstream (KCM) has a reduced amount of spray dried volatiles portion(KBV′) relative to the first volatiles depleted gas stream (KCD).

In embodiments, the second separator (KCI) is a cyclone or a filter.FIG. 17E′ shows the second separator (KCI) as a cyclone. The secondvolatiles depleted gas stream (KCM) is discharged from the secondseparator (KCI) via a second-first output (KCJ).

The second separator (KCI) has: a second-first input (KCK) for receivingthe first volatiles depleted gas stream (KCD) from the first separator(KCA), a second-first output (KCJ) for evacuating the second volatilesdepleted gas stream (KCM) towards the fourth separator (KCZ), and asecond-second output (KCO) for transferring second separated volatiles(KCP) towards the third separator (KCR). The second volatiles depletedgas stream (KCM) is transferred from the second-first output (KCJ) tothe fourth-first input (KDA) of the fourth separator (KCZ) via a thirdtransfer conduit (KCN). The third transfer conduit (KCN) is connected atone end to the second-first output (KCJ) of the second separator (KCI)and at another end to the fourth-first input (KDA) of the fourthseparator (KCZ).

The second separated volatiles (KCP) that are separated from the firstvolatiles depleted gas stream (KCD) are discharged from the secondseparator (KCI) via the second-second output (KCO). The third-firstinput (KCS) of the third separator (KCR) is configured to receive thesecond separated volatiles (KCP) via a second dipleg (KCQ). The seconddipleg (KCQ) is connected at one end to the second-second output (KCO)of the second separator (KCI) and at a second end to the third-firstinput (KCS) of the third separator (KCR). The second separated volatiles(KCP) includes at least a portion of the volatiles that were separatedfrom the first volatiles depleted gas stream (KCD). The second separatedvolatiles (KCP) includes at least a portion of the spray dried volatilesportion (KBV′) that were separated from the first volatiles depleted gasstream (KCD).

The fourth separator (KCZ) separates an additional separated volatiles(KDF) from the second volatiles depleted gas stream (KCM) to create athird volatiles depleted gas stream (KDC). The third volatiles depletedgas stream (KDC) has a reduced amount of volatiles relative to thesecond volatiles depleted gas stream (KCM). The third volatiles depletedgas stream (KDC) has a reduced amount of spray dried volatiles portion(KBV′) relative to the second volatiles depleted gas stream (KCM). Inembodiments, the fourth separator (KCZ) is a cyclone, filter, scrubber,or electrostatic precipitator. In embodiments, the fourth separator(KCZ) is a scrubber that uses second solvent as the scrubbing liquid.

FIG. 17E′ shows the second separator (KCI) as an electrostaticprecipitator. The electrostatic precipitator has an electrode (KM8) anda power supply (KM9) and is configured to separate volatiles from thesecond volatiles depleted gas stream (KCM). The electrode (KM8) and apower supply (KM9) apply an electrostatic charge to the second volatilesdepleted gas stream (KCM) as it passes through the fourth separator(KCZ).

In other embodiments, the fourth separator (KCZ) is a scrubber. Thescrubber, is preferably a vertically oriented cylindrical, orrectangular, pressure vessel having a lower section, and an uppersection, along with a central section that contains a quantity of packedmedia either comprising raschig rings, pall rings, berl saddles, intaloxpacking, metal structured grid packing, hollow spherical packing, highperformance thermoplastic packing, structured packing, synthetic wovenfabric, or ceramic packing, or the like, wherein media is supported upona suitable support grid system commonplace to industrial chemicalequipment systems. The upper section of the scrubber preferably containsa demister to enhance the removal of liquid droplets entrained in avapor stream and to minimize carry-over losses of the sorption liquid.In embodiments, the sorption liquid is second solvent. This demister isalso positioned above the scrubber spray nozzle system, comprised of aplurality of spray nozzles, or spray balls, that introduce andsubstantially equally distribute the scrubbing absorption liquid to thescrubber onto the scrubber's central packing section, so it maygravity-flow down through the scrubber central section.

As the second volatiles depleted gas stream (KCM) passes up through theinternal packing of the scrubber, excess vapor within the additionalseparated volatiles (KDF) comes into intimate contact with scrubbingliquid such as a portion of the second solvent, which are cooled priorto being introduced to the upper section of the scrubber through thescrubber spray nozzle system. Vapor from within the second volatilesdepleted gas stream (KCM) is condensed into a liquid.

The third volatiles depleted gas stream (KDC) is discharged from thefourth separator (KCZ) via a fourth-first input (KDA). The fourthseparator (KCZ) has: fourth-first input (KDA) for receiving the secondvolatiles depleted gas stream (KCM) from the second separator (KCI), afourth-first output (KDB) for evacuating the third volatiles depletedgas stream (KDC) towards the condenser (KDH), and a fourth-second output(KDE) for transferring additional separated volatiles (KDF) towards thethird separator (KCR).

The third volatiles depleted gas stream (KDC) is transferred from thefourth-first output (KDB) to the gas-vapor inlet (KDP) of the condenser(KDH) via a fourth transfer conduit (KDD). The fourth transfer conduit(KDD) is connected at one end to the fourth-second output (KDE) of thefourth separator (KCZ) and at another end to the gas-vapor inlet (KDP)of the condenser (KDH). The additional separated volatiles (KDF) thatare separated from the second volatiles depleted gas stream (KCM) aredischarged from the fourth separator (KCZ) via the fourth-second output(KDE). In embodiments, the third-first input (KCS) of the thirdseparator (KCR) is configured to receive at least a portion of theadditional separated volatiles (KDF) via a fifth transfer conduit (KDG).The fifth transfer conduit (KDG) is connected at one end to thefourth-second output (KDE) of the fourth separator (KCZ) and at a secondend to the third-first input (KCS) of the third separator (KCR).

The third volatiles depleted gas stream (KDC) includes at least aportion of the vapor portion (KBV″) or gas portion (KBV′″) of thevolatiles and gas mixture (KBV) that was discharged from the dryingchamber (KBG). The additional separated volatiles (KDF) includes atleast a portion of the volatiles that were separated from the firstvolatiles depleted gas stream (KCD). The additional separated volatiles(KDF) include at least a portion of the volatiles that were separatedfrom the second volatiles depleted gas stream (KCM). The additionalseparated volatiles (KDF) includes at least a portion of the spray driedvolatiles portion (KBV′) that were separated from the second volatilesdepleted gas stream (KCM).

In embodiments, the additional separated volatiles (KDF) have a sizerange that is selected from one or more from the group consisting of 1nanometer to 5 nanometers, 5 nanometers to 10 nanometers, 10 nanometersto 15 nanometers, 15 nanometers to 20 nanometers, 20 nanometers to 25nanometers, 25 nanometers to 30 nanometers, 30 nanometers to 35nanometers, 35 nanometers to 40 nanometers, 40 nanometers to 45nanometers, 45 nanometers to 50 nanometers, 50 nanometers to 55nanometers, 55 nanometers to 60 nanometers, 60 nanometers to 65nanometers, 65 nanometers to 70 nanometers, 70 nanometers to 75nanometers, 75 nanometers to 80 nanometers, 80 nanometers to 85nanometers, 85 nanometers to 90 nanometers, 90 nanometers to 95nanometers, 95 nanometers to 100 nanometers, 100 nanometers to 200nanometers, 200 nanometers to 300 nanometers, 300 nanometers to 400nanometers, 400 nanometers to 500 nanometers, 500 nanometers to 600nanometers, 600 nanometers to 700 nanometers, 700 nanometers to 800nanometers, and 800 nanometers to 900 nanometers.

In embodiments, the additional separated volatiles (KDF) have a sizerange that is selected from one or more from the group consisting of 1microns to 5 microns, 5 microns to 10 microns, 10 microns to 30 microns,30 microns to 50 microns, 50 microns to 70 microns, 70 microns to 90microns, 90 microns to 110 microns, 110 microns to 130 microns, 130microns to 150 microns, 150 microns to 170 microns, 170 microns to 190microns, 190 microns to 210 microns, 210 microns to 230 microns, and 230microns to 250 microns.

In embodiments, the additional separated volatiles (KDF) have a particlesize distribution (PSD) that has a lesser or smaller PSD relative to thesmall particulate portion (KCW) separated in the solid-solid separator(SSS). In embodiments, the additional separated volatiles (KDF) have aparticle size distribution (PSD) that has a lesser or smaller PSDrelative to the large particulate portion (KCY) separated in thesolid-solid separator (SSS). In embodiments, the particle sizedistribution of the small particulate portion (KCW) is lesser or smallerthan the particle size distribution of the large particulate portion(KCY).

In embodiments, the small particulate portion (KCW) have a size rangethat is selected from one or more from the group consisting of 1 micronsto 5 microns, 5 microns to 10 microns, 10 microns to 30 microns, 30microns to 50 microns, 50 microns to 70 microns, 70 microns to 90microns, 90 microns to 110 microns, 110 microns to 130 microns, 130microns to 150 microns, 150 microns to 170 microns, 170 microns to 190microns, 190 microns to 210 microns, 210 microns to 230 microns, and 230microns to 250 microns.

In embodiments, the large particulate portion (KCY) have a size rangethat is selected from one or more from the group consisting of 50microns to 60 microns, 60 microns to 70 microns, 70 microns to 80microns, 80 microns to 90 microns, 90 microns to 100 microns, 100microns to 150 microns, 150 microns to 200 microns, 200 microns to 250microns, 250 microns to 300 microns, 300 microns to 350 microns, 350microns to 400 microns, 400 microns to 450 microns, 450 microns to 500microns, 500 microns to 550 microns, 550 microns to 600 microns, 600microns to 650 microns, 650 microns to 700 microns, 700 microns to 750microns, 750 microns to 800 microns, 800 microns to 850 microns, 850microns to 900 microns, 900 microns to 950 microns, and 950 microns to1,000 microns.

As shown in FIG. 17E′ the third separator (KCR) accepts first separatedvolatiles (KCG) from the first separator (KCA), and second separatedvolatiles (KCP) from the second separator (KCI), and optionally aportion of the additional separated volatiles (KDF) from the fourthseparator (KCZ), and separates at least a small particulate portion(KCW) and a large particulate portion (KCY) therefrom.

In embodiments, the third separator (KCR) includes solid-solid separator(SSS). In embodiments, the third separator (KCR) includes a sifter asshown in FIG. 17E′. In embodiments, the third separator (KCR) includes afilter. In embodiments, the third separator (KCR) has a third-firstinput (KCS) for receiving: first separated volatiles (KCG) via the firstdipleg (KCH), second separated volatiles (KCP) via the second dipleg(KCQ), and additional separated volatiles (KDF) via the fifth transferconduit (KDG). In embodiments, the third separator (KCR) has athird-first output (KCT) for discharging a third separated volatiles(KCV) which include a small particulate portion (KCW). In embodiments,the small particulate portion (KCW), large particulate portion (KCY),and/or the spray dried volatiles (KBT) may be transferred to themultifunctional composition tank (6F1) on FIG. 18′, or to the cannabistank (6A2) on FIG. 18′.

In embodiments, the third separator (KCR) has a third-second output(KCU) for discharging a fourth separated volatiles (KCX) which include alarge particulate portion (KCY). In embodiments, the large particulateportion (KCY) may be transferred to the cannabis tank (6A2) on FIG. 18′.In embodiments, the third separator (KCR) separates a small particulateportion (KCW) from a large particulate portion (KCY) using a screen(KM3) or a mesh (KM3′). The screen (KM3) or mesh (KM3′) have openings(KM4) that permit the small particulate portion (KCW) to pass throughthe openings (KM4). The openings (KM4) in the screen (KM3) or mesh(KM3′) are too small for the large particulate portion (KCY) to passthrough.

In embodiments, the openings (KM4) in the screen (KM3) or mesh (KM3′)include Unites States Sieve size number 18, 20, 25, 30, 35, 40, 45, 50,60, 70, 80, 100, 120, 140, 170, 200, 230, 270, 325, or 400. Inembodiments, the openings (KM4) in the screen (KM3) or mesh (KM3′) havea size range that is selected from one or more from the group consistingof 37 microns to 44 microns, 44 microns to 53 microns, 53 microns to 63microns, 63 microns to 74 microns, 74 microns to 88 microns, 88 micronsto 105 microns, 105 microns to 125 microns, 125 microns to 149 microns,149 microns to 177 microns, 177 microns to 210 microns, 210 microns to250 microns, 250 microns to 297 microns, 297 microns to 354 microns, 354microns to 420 microns, 420 microns to 500 microns, 500 microns to 595microns, 595 microns to 707 microns, 707 microns to 841 microns, and 841microns to 1,000 microns.

In embodiments, the screen (KM3) or mesh (KM3′) may be cylindrical andlocated within a first chamber (KM5). In embodiments, the thirdseparator (KCR) has a third-first input (KCS) that is configured toreceive particulate volatiles that include first separated volatiles(KCG), second separated volatiles (KCP), and optionally additionalseparated volatiles (KDF). An auger (KM1) is configured to transfer theparticulate volatiles from the third-first input (KCS) to a screen (KM3)or mesh (KM3′) located within the first chamber (KM5) of the thirdseparator (KCR). The auger (KM1) is equipped with a motor (KM2) that maybe operated by the computer (COMP). The particulate volatilestransferred from the third-first input (KCS) are sifted using acylindrical screen (KM3) or mesh (KM3′) that is located within the firstchamber (KM5).

The third-first output (KCT) is located at the bottom of the firstchamber (KM5). The small particulate portion (KCW) may be removed fromthe third separator (KCR) via the third-first output (KCT) located inthe first chamber (KM5). The large particulate portion (KCY) that aretoo large to pass through openings (KM4) of the screen (KM3) or a mesh(KM3′) are transferred from the first chamber (KM5) to the secondchamber (KM6) of the third separator (KCR). Since the openings (KM4) inthe screen (KM3) or mesh (KM3′) within the first chamber (KM5) are toosmall for the large particulate portion (KCY) to pass through, the largeparticulate portion (KCY) is transferred from the first chamber (KM5) tothe second chamber (KM6) of the third separator (KCR). The largeparticulate portion (KCY) are removed from the second chamber (KM6) ofthe third separator (KCR) via the third-second output (KCU).

In embodiments, the sifter is provided by the Kason Corporation. Inembodiments, sifter includes a vibratory screener or a centrifugalsifter. In embodiments, the sifter is provided by Kason Corporation andincludes a VIBRO SCREEN® Circular Vibratory Screener and Separator, aCENTRI-SIFTER™ High Capacity Screener and Separator, a VIBRO-BED™Circular Vibratory Fluid Bed Processor, or a CROSS-FLO High CapacityStatic Sieve Screener and Separator.

In embodiments, the motor (KM2) of the third separator (KCR) is drivenby a belt and ranges from 0.75 horsepower to 6 horsepower. Inembodiments, the motor (KM2) of the third separator (KCR) is driven by abelt and ranges from 0.56 kilowatts to 4.48 kilowatts. In embodiments,the motor (KM2) of the third separator (KCR) is not driven by a belt andranges from 0.5 horsepower to 4 horsepower. In embodiments, the motor(KM2) of the third separator (KCR) is driven by a belt and ranges from0.37 kilowatts to 2.98 kilowatts.

The fourth separator (KCZ) is connected to the condenser (KDH) via afourth transfer conduit (KDD). The third volatiles depleted gas stream(KDC) is transferred through the fourth transfer conduit (KDD) andenters the condenser (KDH). The third volatiles depleted gas stream(KDC) includes the vapor portion (KBV″) and gas portion (KBV′″) thatwere transferred from the spray dryer (KAP).

The condenser (KDH) condenses the vapor portion (KBV″) which may includethe second solvent. Liquid is formed from condensing the vapor portion(KBV″) of the third volatiles depleted gas stream (KDC) to form processcondensate (KDO). Liquid is formed from condensing solvent containedwithin the third volatiles depleted gas stream (KDC) to form processcondensate (KDO). The process condensate (KDO) is discharged from thecondenser (KDH) via a liquid output (KDR).

The gas portion (KBV′″) of the third volatiles depleted gas stream (KDC)is not condensed within the condenser (KDH) and is instead released fromthe condenser (KDH) as a via the gas output (KDQ). The non-condensables(KDT) includes the gas portion (KBV″) of the third volatiles depletedgas stream (KDC) and may include gas, air, nitrogen, carbon dioxide. Thenon-condensables (KDT) leave the gas output (KDQ) of the condenser (KDH)and are routed to a vacuum (KDM) via a gas transfer conduit (KDS).

In embodiments, the vacuum (KDM) is a vacuum pump, fan, or an eductor. Agas exhaust (KDN) is discharged from the vacuum (KDM). The gas exhaust(KDN) includes non-condensables (KDT) or the gas portion (KBV″) of thethird volatiles depleted gas stream (KDC) is not condensed within thecondenser (KDH).

The condenser (KDH) is provided with a cooling water input (KDI) and acooling water output (KDK). The cooling water input (KDI) is configuredto accept a cooling water supply (KDJ) and the cooling water output(KDK) is configured to discharge a cooling water return (KDL). Thecooling water supply (KDJ) is configured to condense a portion of thevapor that enters through the gas-vapor inlet (KDP).

Evaporator Operation: The system shown in FIG. 17E′ can operate in aplurality of modes of operation, including:

(1) preparation of the second volatiles and solvent mixture (SVSM);

(2) start-up;

(3) normal operation;

(4) emergency shut-down;

(5) resuming operations after the emergency shut-down.

As seen in FIG. 17E′, the solvent separation system is equipped with astart-up/shut-down liquid system (KEZ). The purpose of thestart-up/shut-down liquid system (KEZ) is to make a pressurized andoptionally heated supply of liquid immediately available to theevaporator (KAO) whenever necessary. It is preferred that second solvent(SOLV2) is used within the start-up/shut-down liquid system (KEZ), thesecond solvent (SOLV2) includes one or more from the group consisting ofa liquid, acetone, alcohol, oil, ethanol. Water, a first solvent(SOLV1*), or a second solvent (SOLV2*) may be used in thestart-up/shut-down liquid system (KEZ).

In embodiments, the second solvent (SOLV2*) includes one or more fromthe group consisting of petroleum ether, pentane, n-hexane, hexanes,diethyl ether, ethyl acetate, and ethanol. In embodiments, the secondsolvent (SOLV2*) includes one or more from the group consisting ofliquid, acetone, alcohol, oil, ethanol. In embodiments, the secondsolvent (SOLV2*) includes one or more from the group consisting ofpetroleum ether, a heptane, n-heptane, diethyl ether, and methyl tertbutyl ether. In embodiments, the first solvent (SOLV1*) includes one ormore from the group consisting of petroleum ether, a heptane, n-heptane,diethyl ether, and methyl tert butyl ether.

In embodiments, the first solvent (SOLV1*) includes a non-polar solventselected from one or more of the group consisting of pentane, petroleumether, hexanes, n-hexane, heptane, diisopropyl ether, toluene,chloroform, and methylene chloride; preferably petroleum ether, hexanes,n-hexane, heptane, and n-heptane.

In embodiments, the first solvent (SOLV1*) includes a non-polar solventselected from one or more of the group consisting of pentane, petroleumether, hexanes, n-hexane, n-heptane, heptanes, diisopropyl ether,toluene, chloroform, and methylene chloride. In embodiments, the firstsolvent A in the binary solvent system is petroleum ether, a heptane, orn-heptane.

In embodiments, the second solvent (SOLV2*) includes a non-polar solventselected from one or more of the group consisting of pentane, petroleumether, hexanes, n-hexane, heptane, diisopropyl ether, toluene,chloroform, and methylene chloride; preferably petroleum ether, hexanes,n-hexane, heptane, and n-heptane.

In embodiments, the second solvent (SOLV2*) includes a non-polar solventselected from one or more of the group consisting of pentane, petroleumether, hexanes, n-hexane, n-heptane, heptanes, diisopropyl ether,toluene, chloroform, and methylene chloride. In embodiments, the firstsolvent A in the binary solvent system is petroleum ether, a heptane, orn-heptane. It is also desired to be able to mix a known flow of treated,filtered, start-up/shut-down water (KEO) in with the second volatilesand solvent mixture (SVSM) to be used for start-up, shut-down ormaintenance purposes such as cleaning.

A start-up/shut-down liquid tank (KEA) is provided and is configured toaccept a stream of liquid (KEB). The liquid (KEB) transferred to theinterior (KEA′) of the start-up/shut-down liquid tank (KEA) can bepassed through a filter (G23), activated carbon (G24), and/or anadsorbent (G25), and a polishing unit (G41). The polishing unit (G41)may be any type of conceivable device to improve the water quality suchas an ultraviolet unit, ozone unit, microwave unit, filter, adistillation system or the like.

The start-up/shut-down liquid tank (KEA) may be equipped with a levelsensor (KES) that sends a signal (KET) to the computer (COMP). A levelcontrol valve (KEU) may be used to control the amount of liquid (KEB)that is transferred to the interior (KEA′) of the start-up/shut-downliquid tank (KEA). The level control valve (KEU) may be equipped with acontroller (KEV) that is configured to input or output a signal (KEW) tothe computer (COMP). The computer (COMP), level control valve (KEU), andlevel sensor (KES) may be used together in a level control loop tomaintain a constant or batch supply of liquid to the interior (KEA′) ofthe start-up/shut-down liquid tank (KEA).

In embodiments, a start-up heat exchanger (KEP) is configured to heatthe liquid (KEB) that will be transferred to the evaporator (KAO). Inembodiments, a start-up heat exchanger (KEP) is configured to heat theliquid (KEB) that will be transferred to the evaporator (KAO), spraydryer (KAP), rotary atomizer (KAU), spray nozzle (KBC) or plurality ofspray nozzles (KBC), or openings (KBC) or plurality of openings (KBC)within the disc (KBB) of the rotary atomizer (KAU). The purpose ofheating the liquid than will be transferred to the evaporator (KAO) isto not provide a thermal shock on the system while can result in fouledheat transfer surfaces of the outer wall (KWG) within the interior(KBG′) of the drying chamber (KBG), and to prevent cloggage of eitherthe disc (KBB), spray nozzle (KBC), plurality of spray nozzles (KBC),opening (KBD), plurality of openings (KBD), spray aperture (KK4), ororifice (KK5).

Is it desired to heat the liquid (KEO, KEB) that is transferred to thespray dryer (KAP) so that a seamless transition from liquid (KEO, KEB)to a second volatiles and solvent mixture (SVSM) can be realized toattain steady-state conditions in the safest and most efficient manneras possible.

In embodiments, it is necessary to be able to heat the liquid (KEB)prior to adding to the evaporator (KAO) by itself, or add the liquid(KEB) to the evaporator (KAO) together while adding the second volatilesand solvent mixture (SVSM). Herein are disclosed methods to vary theflow of liquid (KEB) to an evaporator, such as a spray dryer, whilevarying either the flow of liquid (KEB) and/or the flow of secondvolatiles and solvent mixture (SVSM) to optimize operations andefficiency while reducing plant maintenance and cleaning.

FIG. 17E′ shows the start-up heat exchanger (KEP) positioned within theinterior (KEA′) start-up/shut-down liquid tank (KEA). In embodiments,the start-up heat exchanger (KEP) is located in between thestart-up/shut-down liquid tank (KEA) and the evaporator (KAO).

In embodiments, a liquid pump (KEK) is provided and configured totransfer liquid from the start-up/shut-down liquid tank (KEA) and intothe evaporator (KAO). The liquid pump (KEK) is equipped with a motor(KEL) and a controller (KEM) which is configured to input or output asignal (KEN) to the computer (COMP).

In embodiments, a liquid control valve (KEF) is provided to control theflow of start-up/shut-down liquid (KEB, KEO) transferred from thestart-up/shut-down liquid tank (KEA) into the evaporator (KAO). Theliquid control valve (KEF) is equipped with a controller (KEG) that isconfigured to input or output a signal (KEH) to the computer (COMP).

In embodiments, a liquid flow sensor (KEI) is provided to measure theflow of start-up/shut-down liquid (KEB, KEO) transferred from thestart-up/shut-down liquid tank (KEA) into the evaporator (KAO). Inembodiments, the computer (COMP), liquid control valve (KEF), liquidflow sensor (KEI), are used in a flow control loop to control the amountof liquid (KEB, KEO) that is provided into the evaporator (KAO).

FIG. 17E′ shows a co-current spray dryer (KAP) evaporator (KAO). In FIG.17E′ the liquid input (KAR) is closer to the top (K-T) than the bottom(K-B). In FIG. 17E′ the gas input (KAQ) is closer to the top (K-T) thanthe bottom (K-B). In FIG. 17E′ the first output (KBS) is closer to thebottom (K-B) than the top (K-T). In FIG. 17E′ the second output (KBU) iscloser to the bottom (K-B) than the top (K-T). Here, the heated gassupply (KAG′) flows in the same direction of the second volatiles andsolvent mixture (SVSM).

FIG. 17E-1′

FIG. 17E-1′ shows one non-limiting embodiment of a co-current type ofspray dryer (KAP) that may be used with the solvent separation systemdescribed in FIG. 17E′.

Shown in FIGS. 17E′, 17E-1′, 17E-2′, 17E-3′, and 17E-4′, are differentembodiments of a spray dryer (KAP) having a top (K-T) bottom (K-B) thatare spaced apart along a vertical axis (KYY). The differences betweenthe different types of spray dryers shown in FIGS. 17E-1′, 17E-2′,17E-3′, and 17E-4′ are the differences in height of various inputs andoutputs, specifically, the differences in relative heights of: (A) theliquid input (KAR) that introduces an second volatiles and solventmixture (SVSM) to the interior (KAP′) of the spray dryer (KAP); (B) thegas input (KAQ) that introduces a heated gas supply (KAG′) to theinterior (KAP′) of the spray dryer (KAP); (C) first output (KB S) thatdischarges volatiles (KBT) from the from the interior (KAP′) of thespray dryer (KAP); and (D) second output (KBU) that evacuates avolatiles and gas mixture (KBV) away from the interior (KAP′) of thespray dryer (KAP).

In FIG. 17E-1′ the liquid input (KAR) is closer to the top (K-T) thanthe bottom (K-B). In FIG. 17E-1′ the gas input (KAQ) is closer to thetop (K-T) than the bottom (K-B). In FIG. 17E-1′ the first output (KBS)is closer to the bottom (K-B) than the top (K-T). In FIG. 17E-1′ thesecond output (KBU) is closer to the bottom (K-B) than the top (K-T).FIG. 17E-1′ shows a co-current spray dryer (KAP) evaporator (KAO) withthe heated gas supply (KAG′) flowing in the same direction of the secondvolatiles and solvent mixture (SVSM).

FIG. 17E-2′

FIG. 17E-2′ shows one non-limiting embodiment of a counter-current typeof spray dryer (KAP) that may be used with the solvent separation systemdescribed in FIG. 17E′.

In FIG. 17E-2′ the liquid input (KAR) is closer to the top (K-T) thanthe bottom (K-B). In FIG. 17E-2′ the gas input (KAQ) is closer to thebottom (K-B) than the top (K-T). In FIG. 17E-2′ the first output (KBS)is closer to the bottom (K-B) than the top (K-T). In FIG. 17E-2′ thesecond output (KBU) is closer to the top (K-T) than the bottom (K-B).FIG. 17E-2′ shows a counter-current spray dryer (KAP) evaporator (KAO)with the heated gas supply (KAG′) flowing in a direction that isopposite to the flow of the second volatiles and solvent mixture (SVSM).Here, the heated gas supply (KAG′) flows upwards from the gas input(KAQ) to the second output (KBU), while the second volatiles and solventmixture (SVSM) is sprayed in a downwards direction.

FIG. 17E-3′

FIG. 17E-3 shows another non-limiting embodiment of a counter-currenttype of spray dryer (KAP) that may be used with the solvent separationsystem described in FIG. 17E.

In FIG. 17E-3 the liquid input (KAR) is closer to the bottom (K-B) thanthe top (K-T). In FIG. 17E-3 the gas input (KAQ) is closer to the top(K-T) than the bottom (K-B). In FIG. 17E-3 the first output (KBS) iscloser to the bottom (K-B) than the top (K-T). In FIG. 17E-3 the secondoutput (KBU) is closer to the bottom (K-B) than the top (K-T).

FIG. 17E-3 shows a counter-current spray dryer (KAP) evaporator (KAO)with the heated gas supply (KAG′) flowing in a direction that isopposite to the flow of the second volatiles and solvent mixture (SVSM).Here, the heated gas supply (KAG′) flows downwards from the gas input(KAQ) to the second output (KBU), while the second volatiles and solventmixture (SVSM) is sprayed in an upwards direction.

FIG. 17E-4′

FIG. 17E-4 shows one non-limiting embodiment of a mixed-flow type ofspray dryer (KAP) that may be used with the solvent separation systemdescribed in FIG. 17E.

In FIG. 17E-4 the liquid input (KAR) is closer to the bottom (K-B) thanthe top (K-T). In FIG. 17E-4 the gas input (KAQ) is closer to the top(K-T) than the bottom (K-B). In FIG. 17E-4 the first output (KBS) iscloser to the bottom (K-B) than the top (K-T). In FIG. 17E-4 the secondoutput (KBU) is second output (KBU) is closer to the bottom (K-B) thanthe top (K-T), the other (KBU′) is closer to the top (K-T) than thebottom (K-B).

FIG. 17E-4 shows a mixed-flow spray dryer (KAP) evaporator (KAO) withthe heated gas supply (KAG′) flowing in a direction that is opposite tothe flow of the second volatiles and solvent mixture (SVSM). Here, theheated gas supply (KAG′) flows both, in the same direction of the secondvolatiles and solvent mixture (SVSM), as well as opposite to thedirection of the flow of the second volatiles and solvent mixture(SVSM). Here, the second volatiles and solvent mixture (SVSM) is sprayedin an upwards direction.

FIG. 17F′

FIG. 17F′ shows a power production system (PPS) that is configured togenerate electricity, heat, or steam for use in the farmingsuperstructure system (FSS).

In embodiments, the power production system (PPS) shown in FIG. 17F′ cangenerate electricity for use in the farming superstructure system (FSS).In embodiments, the power production system (PPS) shown in FIG. 17F′ cangenerate steam and/or heat for use in the farming superstructure system(FSS). In embodiments, the power production system (PPS) shown in FIG.17F′ can generate heat for use in the farming superstructure system(FSS). In embodiments, the power production system (PPS) includes acompressor (LEB), a combustor (LED), a turbine (LFE), a generator (LFH),a HRSG (heat recovery steam generator) (LFI), a steam drum (LBE), asteam distribution header (LCJ), and a condensate tank (LAP). Inembodiments, the turbine (LFE) may be a wind turbine and turns the shaftwith wind power.

An oxygen-containing gas (LEA) is made available to a compressor (LEB).In embodiments, the oxygen-containing gas may be air,oxygen-enriched-air i.e. greater than 21 mole % O2, and substantiallypure oxygen, i.e. greater than about 95 mole % oxygen (the remainderusually comprising N2 and rare gases). In embodiments, theoxygen-containing gas may be flue gas or carbon dioxide. In embodiments,flue gas includes a vapor or gaseous mixture containing varying amountsof nitrogen (N2), carbon dioxide (CO2), water (H2O), and oxygen (O2). Inembodiments, flue gas is generated from the thermochemical process ofcombustion. In embodiments, combustion is an exothermic (releases heat)thermochemical process wherein at least the stoichiometric oxidation ofa carbonaceous material takes place to generate flue gas.

In embodiments, the compressor (LEB) has a plurality of stages (LEC). Inembodiments, the compressor (LEB) is an axial compressor. Inembodiments, the compressor is configured to compress and pressurize theoxygen-containing gas (LEA) to form a compressed gas stream (LEK). Inembodiments, the compressor is configured to compress and pressurize theoxygen-containing gas (LEA) to form a first compressed gas stream (LEK)and a second compressed gas stream (LEN). In embodiments, compressed gasstream (LEK) is provided to a combustor (LED). In embodiments, the firstcompressed gas stream (LEK) is provided to a first combustor (LED1). Inembodiments, the second compressed gas stream (LEN) is provided to asecond combustor (LED2).

In embodiments, the first combustor (LED1) has a first gas mixer (LEE).In embodiments, the second combustor (LED2) has a second gas mixer(LEH). In embodiments, the first gas mixer (LEE) or second gas mixer(LEH) is that of an annular type. In embodiments, the first combustor(LED1) or second combustor (LED2) is that of an annular type. Inembodiments, the annular type gas mixer (LEE) mixes the fuel with theoxygen containing-gas within the combustor to form afuel-and-oxygen-containing gas mixture, which is then combusted. Inembodiments, the first combustor (LED1) has a first ignitor (LEF). Inembodiments, the second combustor (LED2) has a second ignitor (LEI). Inembodiments, the first ignitor (LEF) or second ignitor (LEI) include atorch ignitor. In embodiments, the first ignitor (LEF) or second ignitor(LEI) include a separate fuel supply to maintain a constantly burningtorch. In embodiments, the first combustor (LED1) has a first flamedetector (LEG). In embodiments, the second combustor (LED2) has a secondflame detector (LEJ). In embodiments, the first flame detector (LEG) orsecond flame detector (LEJ) are selected from one or more from the groupconsisting of a UV flame detector, IR flame detector, UV/IR flamedetector, multi-spectrum infrared flame detector, and a visual flameimaging flame detector.

In embodiments, the combustor (LED) mixes and combusts the compressedgas stream (LEK) with a first fuel (LEL) to produce a combustion stream(LEM). In embodiments, the first combustor (LED1) mixes and combusts thefirst compressed gas stream (LEK) with a first fuel (LEL) to produce afirst combustion stream (LEM). In embodiments, the first combustionstream (LEM) is a first pressurized combustion stream (LEM′). Inembodiments, the second combustor (LED2) mixes and combusts the secondcompressed gas stream (LEN) with a second fuel (LEO) to produce a secondcombustion stream (LEP). In embodiments, the second combustion stream(LEP) is a second pressurized combustion stream (LEP′).

A first fuel valve (LEW) is provided to regulate the flow of thecompressor fuel source (LEU) to the first combustor (LED1) and thesecond combustor (LED2). The first fuel valve (LEW) is equipped with acontroller (LEX) that is configured to input or output a signal (LEY) tothe computer (COMP). FIG. 17F′ shows connector (K1) to show continuitybetween the second fuel (LEO) that is apportioned from the compressorfuel source (LEU) and transferred to the second combustor (LED2).

The combustion stream (LEM) is transferred to a turbine (LFE). Inembodiments, the first combustion stream (LEM) is combined with thesecond combustion stream (LEP) before being transferred to the turbine(LFE). In embodiments, the turbine (LFE) has a plurality of stages(LFF). In embodiments, the first and second combustion streams (LEM,LEP) rotate a portion of the turbine (LFE), which in turn rotates ashaft (LFG), and a generator (LFH) to produce electricity (ELEC). Inembodiments, the combustion stream (LEM) rotates the turbine (LFE),which in turn rotates a shaft (LFG), and a generator (LFH) to produceelectricity (ELEC).

In embodiments, the compressor (LEB) is connected to the turbine (LFE)via a shaft (LFG). In embodiments, the turbine (LFE) is connected to thegenerator (LFH) via a shaft (LFG). In embodiments, the turbine (LFE)rotates the shaft (LFG) which in turn drives the compressor (LEB). Inembodiments, the generator (LFH) is connected to the turbine (LFE) via ashaft (LFG). In embodiments, the turbine (LFE) rotates the shaft (LFG)which in turn drives the generator (LFH) to produce electricity for usein the farming superstructure system (FSS).

FIG. 17F′ shows the generator (LFH) producing electricity for use in thecomputer (COMP) within the farming superstructure system (FSS). Inembodiments, the electricity (ELEC) may be used in the farmingsuperstructure system (FSS) in any number of a plurality of: sensors,motors, pumps, heat exchangers, fans, actuators, controllers,compressors, analyzers, computers, lights, heaters, vacuum pumps, etc.Any asset, including sensors, motors, pumps, heat exchangers, fans,actuators, controllers, compressors, analyzers, computers, lights,heaters, vacuum pumps, disclosed in FIGS. 1A through 23 may be poweredby the electricity (ELEC) generated by the generator (LFH) or generator(LCA).

A combustion stream (LFD) is discharged from the turbine (LFE) and isrouted to a HRSG (LFI). In embodiments, the combustion stream (LFD) thatis discharged from the turbine (LFE) is a depressurized combustionstream (LFD′). In embodiments the depressurized combustion stream (LFD′)has a pressure that is less than the pressure of the combustion stream(LEM, LEP) that is transferred to the turbine (LFE). The combustionstream (LFD) is transferred from the turbine (LFE) to the HRSG (LFI).The HRSG (LFI) is configured to remove heat from the combustion stream(LFD) by use of a heat transfer conduit (LBI) or a plurality of heattransfer conduits (LBI). At least one heat transfer conduit (LBI)generates steam through indirect heat transfer from the combustionstream (LFD).

In embodiments, the HRSG (LFI) is a fired-HRSG (LFJ). In embodiments,the fired-HRSG (LFJ) accepts a HRSG fuel source (LEV). In embodiments,the HRSG fuel source (LEV) is combusted with the combustion stream (LFD)that is transferred from the turbine (LFE) to form a combustion stream(LX0′). In embodiments, the HRSG fuel source (LEV) is combusted with anoxygen-containing gas (LX0). In the instance where the HRSG fuel source(LEV) is combusted with an oxygen-containing gas (LX0), the compressor(LEB), a combustor (LED), a turbine (LFE), a generator (LFH) areoptional. Thus, saturated steam (LBR) or superheated steam (LBS) may begenerated within the steam drum (LBE) by combusting an oxygen-containinggas (LX0) with the compressor fuel source (LEU) to form a combustionstream (LX0′).

In embodiments, a second fuel valve (LFA) is made available to regulatethe amount of the HRSG fuel source (LEV) that is introduced to thefired-HRSG (LFJ). The second fuel valve (LFA) is equipped with acontroller (LFB) that is configured to input or output a signal (LFC) tothe computer (COMP). In embodiments, the compressor fuel source (LEU)and HRSG fuel source (LEV) come from a common fuel source (LEQ). Acompressor fuel source (LEU) provides the fuel that is used as the firstfuel (LEL) and second fuel (LEO). In embodiments, the fuel source (LEQ)that is made available as the compressor fuel source (LEU) or HRSG fuelsource (LEV) may include a hydrocarbon. In embodiments, the fuel source(LEQ) that is made available as the compressor fuel source (LEU) or HRSGfuel source (LEV) may be a liquid, vapor, or a gas. In embodiments, thefuel source (LEQ) that is made available as the compressor fuel source(LEU) or HRSG fuel source (LEV) may be a methane containing gas such asnatural gas. In embodiments, the fuel source (LEQ) that is madeavailable as the compressor fuel source (LEU) or HRSG fuel source (LEV)may be naphtha, natural gas, gasoline, a hydrocarbon, diesel, or oil. Inembodiments, the fuel source (LEQ, LET, LEU, LEV), may include ahydrocarbon, and may be a liquid, vapor, or a gas. In embodiments, thefuel source (LEQ, LET, LEU, LEV), may be a methane containing gas suchas natural gas, or otherwise may be naphtha, natural gas, gasoline, ahydrocarbon, diesel, or oil.

In embodiments, a fuel source (LEQ) is made available to a fuelcompressor (LER) to form a compressed fuel (LET). In embodiments, thefuel compressor (LER) has a plurality of stages (LES). A pressure sensor(LEQP) is provided to measure the pressure of the fuel source (LEQ) thatis made available to the fuel compressor (LER). In embodiments, thecompressor fuel source (LEU) and HRSG fuel source (LEV) are a compressedfuel (LET). In embodiments, the HRSG fuel source (LEV) is combustedwithin the fired-HRSG (LFJ) using a burner (LFK) such as a duct burner.In embodiments, the fired-HRSG (LFJ) or the burner (LFK) is lined withrefractory material. In embodiments, the refractory material includes aceramic, alumina, silica, magnesia, silicon carbide, or graphite.

In embodiments, heat is removed from the HRSG (LFI) and a flue gas (LFP)is evacuated from the HRSG (LFI). In embodiments, heat is removed fromthe fired-HRSG (LFJ) and a flue gas (LFP) is evacuated from thefired-HRSG (LFJ). A temperature sensor (LFM) is configured to measurethe temperature within the HRSG (LFI, LFJ). A temperature sensor (LFM)is configured to measure the temperature of the flue gas (LFP) that isdischarged from the HRSG (LFI, LFJ).

In embodiments, at least a portion of the flue gas (LFP) is madeavailable as flue gas (FG1) that may be transferred to the thermalcompressor (Q30) on FIG. 5C′ or 5E′. In embodiments, at least a portionof the flue gas (LFP) is made available as flue gas (FG1) that may betransferred to the generator (Q50) within the thermal compressor (Q30)on FIG. 5C′ or 5E′.

The steam generated in the plurality of heat transfer conduits (LBI) isrouted to a steam drum (LBE). In embodiments, the steam drum (LBE)generates saturated steam (LBR) or superheated steam (LBS). Inembodiments, saturated steam (LBR) is discharged from the steam drum(LBE) and is routed to a superheater (LX3) through a saturated steamtransfer conduit (LX1). Heat is transferred from the combustion stream(LFD, LX0′) to saturated steam (LBR) within the superheater (LX3) toproduce superheated steam (LBS) which is routed to a superheated steamtransfer conduit (LX2).

A steam distribution header (LCJ) is configured to accept at least aportion of the saturated steam (LBR) or superheated steam (LBS). Inembodiments, a first portion (LBW) of either the saturated steam (LBR)or superheated steam (LBS) is transferred through a first steam transferconduit (LBY) and into the steam distribution header (LCJ). Inembodiments, a second portion (LBX) of either the saturated steam (LBR)or superheated steam (LBS) is transferred through a second steamtransfer conduit (LSY) and into steam turbine (LBZ) to generateelectricity via a generator (LCA). In embodiments, the steam turbine(LBZ) has a plurality of stages (LBZX). The steam turbine (LBZ) isconnected to a generator (LCA) via a shaft (LCB). Depressurized steam(LCI) is evacuated from the steam turbine (LBZ) and is routed towardsthe steam distribution header (LCJ).

FIG. 17F′ shows a steam distribution header (LCJ) that is configured toaccept at least a portion of the saturated steam (LBR) or superheatedsteam (LBS) that are routed through either the first steam transferconduit (LBY) or second steam transfer conduit (LSY). A pressure sensor(LBO) is provided to measure the pressure within the interior of thesteam drum (LBE). A temperature sensor (LBQ) is provided to measure thetemperature of the saturated steam (LBR) or superheated steam (LBS) thatare discharged from the steam drum (LBE). A pressure control valve (LBT)is positioned on the steam distribution header (LCJ). In embodiments,the pressure control valve (LBT) controls the pressure within the steamdrum (LBE). In embodiments, the pressure control valve (LBT) controlsthe pressure within first steam transfer conduit (LBY) and second steamtransfer conduit (LSY). The pressure control valve (LBT) is equippedwith a controller (LBU) that sends a signal (LBV) to or from thecomputer (COMP). In embodiments, the computer (COMP), pressure controlvalve (LBT), and pressure sensor (LBO) are used in a control loop toregulate the pressure within the steam drum (LBE), first steam transferconduit (LBY), or second steam transfer conduit (LSY).

In embodiments, the steam distribution header (LCJ) provides a source ofsteam to a variety of locations within the farming superstructure system(FSS). In embodiments, the velocity of steam within the steamdistribution header (LCJ) ranges from one or more from the groupselected from 50 feet per second (FPS) to 60 FPS, 60 FPS to 70 FPS, 70FPS to 80 FPS, 80 FPS to 90 FPS, 90 FPS to 100 FPS, 100 FPS to 110 FPS,110 FPS to 120 FPS, 120 FPS to 130 FPS, 130 FPS to 140 FPS, 140 FPS to150 FPS, 150 FPS to 160 FPS, 160 FPS to 180 FPS, 180 FPS to 200 FPS, 200FPS to 225 FPS, and 225 FPS to 250 FPS.

In embodiments, the steam distribution header (LCJ) operates at apressure range that is selected from one or more from the groupconsisting of 5 pounds per square inch (PSI) 10 PSI, 10 PSI 20 PSI, 20PSI 30 PSI, 30 PSI 40 PSI, 40 PSI 50 PSI, 50 PSI 60 PSI, 60 PSI 70 PSI,70 PSI 80 PSI, 80 PSI 90 PSI, 90 PSI 100 PSI, 100 PSI 125 PSI, 125 PSI150 PSI, 150 PSI 175 PSI, 175 PSI 200 PSI, 200 PSI 225 PSI, 225 PSI 250PSI, 250 PSI 275 PSI, 275 PSI 300 PSI, 300 PSI 325 PSI, 325 PSI 350 PSI,350 PSI 375 PSI, 375 PSI 400 PSI, 400 PSI 425 PSI, 425 PSI 450 PSI, 450PSI 475 PSI, 475 PSI 500 PSI, 500 PSI 525 PSI, 525 PSI 550 PSI, 550 PSI575 PSI, 575 PSI 600 PSI, 600 PSI 700 PSI, 700 PSI 800 PSI, 800 PSI 900PSI, and 900 PSI 1,000 PSI.

In embodiments, the steam distribution header (LCJ) is insulated withinsulation (LCJ′). In embodiments, the range of thickness of theinsulation (LCJ′) on the steam distribution header (LCJ) is selectedfrom one or more from the group consisting of 1 inches to 1.5 inches,1.5 inches to 2 inches, 2 inches to 2.5 inches, 2.5 inches to 3 inches,3 inches to 3.5 inches, 3.5 inches to 4 inches, 4 inches to 4.5 inches,4.5 inches to 5 inches, 5 inches to 5.5 inches, 5.5 inches to 6 inches,6 inches to 6.5 inches, 6.5 inches to 7 inches, 7 inches to 7.5 inches,7.5 inches to 8 inches, 8 inches to 8.5 inches, 8.5 inches to 9 inches,9 inches to 9.5 inches, 9.5 inches to 10 inches, 10 inches to 11 inches,11 inches to 12 inches, 12 inches to 13 inches, 13 inches to 14 inches,14 inches to 15 inches, 15 inches to 16 inches, 16 inches to 17 inches,and 17 inches to 18 inches.

In embodiments, the steam distribution header (LCJ) provides a source ofsteam to a variety of locations including: a first steam supply (LCL) toFIG. 5C′ to the thermal compressor (Q30), a second steam supply (LCL) toFIG. 17D′ to the evaporator (J11), a third steam supply (LCL) to FIG.17E′ to the spray dryer (KAP), a fourth steam supply (LCL) to FIG. 17E′to the spray dryer (KAP) heating jacket (KBJ).

In embodiments, a first steam valve (LCM) is configured to regulate theamount of the first steam supply (LCL) to FIG. 5C′ to the thermalcompressor (Q30). A first reducer (LCN) may be positioned upstream ordownstream of the first steam valve (LCM) on the steam distributionheader (LCJ).

In embodiments, a second steam valve (LDK) is configured to regulate theamount of the second steam supply (LDJ) to FIG. 17D′ to the evaporator(J11). A second reducer (LDL) may be positioned upstream or downstreamof the second steam valve (LDK) on the steam distribution header (LCJ).

In embodiments, a third steam valve (LDN) is configured to regulate theamount of the third steam supply (LDM) to FIG. 17E′ to the spray dryer(KAP). A third reducer (LDO) may be positioned upstream or downstream ofthe third steam valve (LDN) on the steam distribution header (LCJ).

In embodiments, a fourth steam valve (LDQK) is configured to regulatethe amount of the fourth steam supply (LDP) to FIG. 17E′ to the spraydryer (KAP) heating jacket (KBJ). A fourth reducer (LDR) may bepositioned upstream or downstream of the fourth steam valve (LDQ) on thesteam distribution header (LCJ).

In turn, a plurality of steam condensate streams are transferred fromvarious locations within the FSS and are returned to a condensate tank(LAP) as indicated on FIG. 17F′. In embodiments, the condensate tank(LAP) accepts steam condensate streams are transferred from variouslocations, including: a first condensate (LJC) from FIG. 5C′ from thethermal compressor (Q30), a second condensate (LAW) from FIG. 17D′ fromthe evaporator (J11), a third condensate (LJA) from FIG. 17E′ from thespray dryer (KAP), a fourth condensate (LJB) from FIG. 17E′ from thespray dryer (KAP) heating jacket (KBJ).

In embodiments, at least a portion are used again to remove heat withinthe HRSG (LFI, LFJ): first condensate (LJC), second condensate (LAW),third condensate (LJA), fourth condensate (LJB). In embodiments, feedwater (LAX) (which may include condensate (LJC, LAW, LJA, LJB)) ispumped to the from the condensate tank (LAP) to the steam drum input(LBD) of the steam drum (LBE) via a pump (LAX′).

A heat exchanger (LAZ) is provided to pre-heat the feed water (LAX) asit is transferred from the condensate tank (LAP) to the steam drum(LBE). A temperature sensor (LAY) is provided to measure the temperatureof the feed water (LAX) before it enters the heat exchanger (LAZ).Another temperature sensor (LBC) is provided to measure the temperatureof the feed water (LAX) after is exits the heat exchanger (LAZ).

In embodiments, the steam drum (LBE) is equipped with a level sensor(LBP) that is configured to regulate the amount of feed water (LAX) thatis introduced to the steam drum (LBE). In embodiments, the steam drum(LBE) is equipped with a level control valve (LBP′) that is configuredto regulate the amount of feed water (LAX) that is introduced to thesteam drum (LBE). In embodiments, the computer (COMP), level sensor(LBP), and level control valve (LBP′) may be used in a control loop toregulate the amount of feed water (LAX) that is introduced to the steamdrum (LBE).

In embodiments, the steam drum (LBE) is connected to a lower steam drum(LBF) via a plurality of heat transfer conduit (LBG, LBH, LBI). Inembodiments, lower steam drum (LBF) is configured to discharge ablowdown (LBK) through a valve (LBN). In embodiments, the blowdown (LBK)includes suspended solids (LBL) and/or dissolved solids (LBM). Inembodiments, the suspended solids (LBL) include solids such as bacteria,silt and mud. In embodiments, the dissolved solids (LBM) may includeminerals, salts, metals, cations or anions dissolved in water. Inembodiments, the dissolved solids (LBM) include inorganic saltsincluding principally calcium, magnesium, potassium, sodium,bicarbonates, chlorides, and sulfates.

In embodiments, the condensate tank (LAP) also serves the purpose as awater tank (LAO) for accepting treated water (LAJ). Thus, treated water(LAJ) is added to the condensate tank (LAP) to make-up for water lossesin the system. A source of water (LAA) is made available to a series ofunit operations that are configured to improve the water. Inembodiments, the source of water (LAA) is passed through a filter (LAC),a packed bed (LAD) of adsorbent (LAE), a cation (LAF), an anion (LAG), amembrane (LAH), followed by another cation/anion (LAI) to result intreated water (LAJ).

The treated water (LAJ) is then provided to the condensate tank(LAP)/water tank (LAO) via a pump (LAK). In embodiments, the treatedwater (LAJ) that is transferred to the condensate tank (LAP)/water tank(LAO) via a pump (LAK) is passed through a valve (LAL). The valve (LAL)is equipped with a controller (LAM) that is configured to input oroutput a signal (XAM) to the computer (COMP). A quality sensor (LAN) isprovided as a quality control of the unit operations that are configuredto improve the water.

FIG. 17G′

FIG. 17G′ shows one non-limiting embodiment of a carbon dioxide removalsystem (GAE) that is configured to remove carbon dioxide from flue gas(LFP) for use as a source of carbon dioxide (CO2) in the farmingsuperstructure system (FSS).

Flue gas (LFP) is provided from FIG. 17F′ to FIG. 17G. The flue gas(LFP) is routed to a first compressor (GAB), which may have a pluralityof stages (GAC). A first pressure sensor (GAA) measures the inletpressure to the first compressor (GAB). The first compressor (GAB)elevates the pressure of the flue gas to produce pressurized flue gas(GAD). A second pressure sensor (GAA) measures the outlet pressure tothe first compressor (GAB). A carbon dioxide removal system (GAE) isprovided to remove carbon dioxide (CO2) from flue gas (LFP) or from thepressurized flue gas (GAD). A carbon dioxide depleted flue gas isdischarged from the carbon dioxide removal system (GAE). In embodiments,the carbon dioxide (CO2) that was removed from the flue gas (LFP, GAD)is provided to the carbon dioxide tank (CO2T), which is discussed indetail on FIGS. 1A and 1B. Alternately, the carbon dioxide (CO2) thatwas removed from the flue gas (LFP, GAD) may be directly made availableto the first growing assembly (100) or second growing assembly (200).

In embodiments, carbon dioxide removal system (GAE) may include one ormore from the group consisting of a membrane, an adsorber, a pressureswing adsorber, a temperature swing adsorber, a membrane, a solventscrubber, a scrubber, an absorber, an amine scrubber, and an amineabsorber.

In embodiments, the an adsorber, fixed bed adsorber, moving bedadsorber, a pressure swing adsorber, a temperature swing adsorber, maycontain an adsorbent material. In embodiments, the adsorbent materialmay include regenerable and non-regenerable sorbents. In embodiments,the adsorbent material may be selected from one or more from the groupconsisting of 3 Angstrom molecular sieve, 3 Angstrom zeolite, 4 Angstrommolecular sieve, 4 Angstrom zeolite, activated alumina, activatedcarbon, adsorbent, alumina, carbon, catalyst, clay, desiccant, molecularsieve, zeolites, polymer, resin, and silica gel.

In embodiments, a second compressor (GAG) is provided to compress thecarbon dioxide that is discharged from the carbon dioxide removal system(GAE). The second compressor (GAG) elevates the pressure of the carbondioxide to produce carbon dioxide (GAI). In embodiments, the secondcompressor (GAG) has a plurality of stages (GAH).

As shown in FIG. 17G′, the carbon dioxide tank (CO2T) is in fluidcommunication with the plurality of growing assemblies (100, 200) asshown on FIGS. 1A′ and 1B′. The carbon dioxide tank (CO2T) containspressurized carbon dioxide (CO2) and is equipped with a carbon dioxidepressure sensor (CO2P). A carbon dioxide supply header (CO2H) isconnected to the carbon dioxide tank (CO2T). A first carbon dioxidesupply valve (V10) is installed on the carbon dioxide supply header(CO2H) and is configured to take a pressure drop of greater than 50pounds per square inch (PSI). In embodiments, range of the pressure dropacross the first carbon dioxide supply valve (V10) is selected from oneor more from the group consisting of 25 pounds per square inch (PSI) to50 PSI, 50 PSI to 75 PSI, 75 PSI to 100 PSI, 100 PSI to 125 PSI, 125 PSIto 150 PSI, 150 PSI to 175 PSI, 175 PSI to 200 PSI, 200 PSI to 225 PSI,225 PSI to 250 PSI, 250 PSI to 275 PSI, 275 PSI to 300 PSI, 300 PSI to325 PSI, 325 PSI to 350 PSI, 350 PSI to 375 PSI, 375 PSI to 400 PSI, 400PSI to 425 PSI, 425 PSI to 450 PSI, 450 PSI to 475 PSI, 475 PSI to 500PSI, 500 PSI to 600 PSI, 600 PSI to 700 PSI, 700 PSI to 800 PSI, 800 PSIto 900 PSI, 900 PSI to 1000 PSI, 1,000 PSI to 1,250 PSI, 1,250 PSI to1,500 PSI, 1,500 PSI to 1,750 PSI, 1,750 PSI to 2,000 PSI, 2,000 PSI to2,250 PSI, 2,250 PSI to 2,500 PSI, 2,500 PSI to 2,750 PSI, 2,750 PSI to3,000 PSI, 3,000 PSI to 3,250 PSI, 3,250 PSI to 3,500 PSI, 3,500 PSI to3,750 PSI, 3,750 PSI to 4,000 PSI, 4,000 PSI to 4,500 PSI, and 4,500 PSIto 5,000 PSI.

As shown in FIGS. 1A′ and 13, the carbon dioxide (CO2) transferred fromthe carbon dioxide tank (CO2T) the first growing assembly (100) isequipped with a CO2 input (115) that is connected to a CO2 supplyconduit (116). The second growing assembly (200) is also equipped with aCO2 input (215) that is connected to a CO2 supply conduit (216). The CO2supply conduit (116) of the first growing assembly (100) is connected tothe carbon dioxide supply header (CO2H) via a CO2 header connection(115X). The CO2 supply conduit (116) of the first growing assembly (100)is configured to transfer carbon dioxide into the first interior (101)of the first growing assembly (100). In embodiments, a second carbondioxide supply valve (V8) is installed on the CO2 supply conduit (116)of the first growing assembly (100). The second carbon dioxide supplyvalve (V8) is equipped with a controller (CV8) that sends a signal (XV8)to and from a computer (COMP). In embodiments, a CO2 flow sensor (FC1)is installed on the CO2 supply conduit (116) of the first growingassembly (100). The CO2 flow sensor (FC1) sends a signal (XFC1) to thecomputer (COMP). In embodiments, a gas quality sensor (GC1) is installedon the first growing assembly (100) to monitor the concentration ofcarbon dioxide within the first interior (101). The gas quality sensor(GC1) is equipped to send a signal (XGC1) to the computer (COMP).

The CO2 supply conduit (216) of the second growing assembly (200) isconnected to the carbon dioxide supply header (CO2H) via a CO2 headerconnection (215X). The CO2 supply conduit (216) of the second growingassembly (200) is configured to transfer carbon dioxide into the secondinterior (201) of the second growing assembly (100). In embodiments, athird carbon dioxide supply valve (V9) is installed on the CO2 supplyconduit (216) of the second growing assembly (200). The third carbondioxide supply valve (V9) is equipped with a controller (CV9) that sendsa signal (XV9) to and from a computer (COMP). In embodiments, a CO2 flowsensor (FC2) is installed on the CO2 supply conduit (216) of the secondgrowing assembly (200). The CO2 flow sensor (FC2) sends a signal (XFC2)to the computer (COMP). In embodiments, a gas quality sensor (GC2) isinstalled on the second growing assembly (200) to monitor theconcentration of carbon dioxide within the second interior (201). Thegas quality sensor (GC2) is equipped to send a signal (XGC2) to thecomputer (COMP).

In embodiments, the range of the carbon dioxide concentration in theplurality of growing assemblies (100, 200) is selected from one or morefrom the group consisting of 390 part per million (PPM) to 400 PPM, 400PPM to 410 PPM, 410 PPM to 420 PPM, 420 PPM to 430 PPM, 430 PPM to 440PPM, 440 PPM to 450 PPM, 450 PPM to 460 PPM, 460 PPM to 470 PPM, 470 PPMto 480 PPM, 480 PPM to 490 PPM, 490 PPM to 500 PPM, 500 PPM to 510 PPM,510 PPM to 520 PPM, 520 PPM to 530 PPM, 530 PPM to 540 PPM, 540 PPM to550 PPM, 550 PPM to 560 PPM, 560 PPM to 570 PPM, 570 PPM to 580 PPM, 580PPM to 590 PPM, 590 PPM to 600 PPM, 600 PPM to 620 PPM, 620 PPM to 640PPM, 640 PPM to 660 PPM, 660 PPM to 680 PPM, 680 PPM to 700 PPM, 700 PPMto 720 PPM, 720 PPM to 740 PPM, 740 PPM to 760 PPM, 760 PPM to 780 PPM,780 PPM to 800 PPM, 800 PPM to 820 PPM, 820 PPM to 840 PPM, 840 PPM to860 PPM, 860 PPM to 880 PPM, 880 PPM to 900 PPM, 900 PPM to 920 PPM, 920PPM to 940 PPM, 940 PPM to 960 PPM, 960 PPM to 980 PPM, 980 PPM to 1000PPM, 1,000 PPM to 1,500 PPM, 1,500 PPM to 2,000 PPM, 2,000 PPM to 2,500PPM, 2,500 PPM to 3,000 PPM, 3,000 PPM to 3,500 PPM, 3,500 PPM to 4,000PPM, 4,000 PPM to 4,500 PPM, 4,500 PPM to 5,000 PPM, 5,000 PPM to 5,500PPM, 5,500 PPM to 6,000 PPM, 6,000 PPM to 6,500 PPM, 6,500 PPM to 7,000PPM, 7,000 PPM to 7,500 PPM, 7,500 PPM to 8,000 PPM, 8,000 PPM to 8,500PPM, 8,500 PPM to 9,000 PPM, 9,000 PPM to 9,500 PPM, 9,500 PPM to 10,000PPM, 10,000 PPM to 11,000 PPM, 11,000 PPM to 12,000 PPM, 12,000 PPM to13,000 PPM, 13,000 PPM to 14,000 PPM, 14,000 PPM to 15,000 PPM, 15,000PPM to 16,000 PPM, 16,000 PPM to 17,000 PPM, 17,000 PPM to 18,000 PPM,18,000 PPM to 19,000 PPM, 19,000 PPM to 20,000 PPM, 20,000 PPM to 21,000PPM, 21,000 PPM to 22,000 PPM, 22,000 PPM to 23,000 PPM, 23,000 PPM to24,000 PPM, and 24,000 PPM to 25,000 PPM.

FIG. 17H′

FIG. 17H′ shows a cannabinoid extraction system including vessels,filters, pumps, piping connecting flow between vessels and adsorbers,valving, controllers, pressure regulators, metering equipment, flowcontrol, and microprocessor equipment, their construction,implementation, and functionality.

FIG. 17H′ shows one non-limiting embodiment of a solvent separationsystem that is configured to adsorb and desorb at least a portion ofvolatiles from a volatiles and solvent mixture (SVSM) by use of aplurality of adsorbers that contain an adsorbent. In embodiments,volatiles include cannabinoids. FIGS. 17H′, 17J′, and 17K′ shownon-limiting schematics of process flow diagrams illustratingconfigurations of a continuous cannabinoid extraction, emulsification,and softgel encapsulation system including:

-   -   cannabis drying system;    -   water treatment and pH adjustment system;    -   cannabinoid extraction system;    -   primary solvent filtration system;    -   primary cannabinoid adsorption system;    -   secondary solvent filtration system;    -   secondary cannabinoid adsorption system;    -   tertiary solvent filtration system;    -   tertiary cannabinoid adsorption system;    -   solvent recovery system;    -   cannabinoid product processing (emulsion mixing system,        evaporation system, spray drying system, crystallization,        foodstuff preparation system, softgel encapsulation system).

Disclosed is a continuous process for the purification of cannabidioland/or tetrahydrocannabinol extracted from cannabis using continuoussimulated moving bed processes and micro and nanofiltration without theaddition of organic solvents to obtain a purified cannabidiol and/ortetrahydrocannabinol product. The cannabidiol and/ortetrahydrocannabinol can be used to create foodstuffs, emulsions, drugs,beverages, alcoholic beverages or for medicinal or recreational uses,and pet food.

In embodiments, a method for purification and separation of cannabidioland/or tetrahydrocannabinol from cannabis and continuous purification ofcannabidiol and/or tetrahydrocannabinol is disclosed. More particularly,the method relates to a process for the continuous purification ofcannabidiol and/or tetrahydrocannabinol from cannabis using simulatedmoving bed chromatography. Most particularly, the method relates to anovel continuous process for the purification of cannabidiol and/ortetrahydrocannabinol from cannabis using a continuous simulated movingbed process using a solvent (such as water, ethanol, an alcohol, analcohol mixture, deionized water, treated water, membrane treated water)as the mobile phase desorbent without the addition of organic solventsto obtain a purified cannabidiol and/or tetrahydrocannabinol productcomprising cannabidiol and/or tetrahydrocannabinol. The cannabidioland/or tetrahydrocannabinol can be used to create foodstuffs, emulsions,drugs, beverages, alcoholic beverages or for medicinal or recreationaluses, and pet foods.

In embodiments, cannabis or DANLEO III contains cannabinoids. Inembodiments, cannabinoids are contained within volatiles. Inembodiments, cannabinoids include cannabidiol and tetrahydrocannabinol.In embodiments, cannabinoids include Δ9-tetrahydrocannabinol Δ9-THC,Δ8-tetrahydrocannabinol Δ8-THC, cannabichromene CBC, cannabidiol CBD,cannabigerol CBG, cannabinidiol CBND, and/or cannabinol CBN. Inembodiments, tetrahydrocannabinol has a molecular weight of 314.47 gramsper mole. In embodiments, cannabidiol has a molecular weight of 314.47grams per mole.

The cannabinoids within cannabis or DANLEO III are listed below and bearthe IUPAC names(6aR-trans)-6a,7,8,10a-tetrahydro-6,6,9-trimethyl-3-pentyl-6H-dibenzo[b,d]pyran-1-olor Δ9-THC, and(6aR-trans)-6a,7,10,10a-tetrahydro-6,6,9-trimethyl-3-pentyl-6H-dibenzo[b,d]pyran-1-olor Δ8-THC. Δ9-THC is also known under the designation of Dronabinol.

Table 17H′ illustrates various cannabinoids that are contained withincannabis or DANLEO III: Δ9-tetrahydrocannabinol Δ9-THC,Δ8-tetrahydrocannabinol Δ8-THC, cannabichromene CBC, cannabidiol CBD,cannabigerol CBG, cannabinidiol CBND, and/or cannabinol CBN.

Cannabinoids can be extracted from leaves, buds, stems, and/orvolatiles, of cannabis or DANLEO III with use of a solvent, the solventincludes one or more from the group consisting of acetone, alcohol,ethanol, methanol, hexane, insect lipids, isobutane, isopropanol, liquidcarbon dioxide, liquid, naphtha, and water. Cannabinoids can beextracted from volatiles that were separated from the cannabis or DANLEOIII by use of carbon dioxide. In embodiments, carbon dioxide extractedvolatiles contain cannabinoids. In embodiments, carbon dioxide extractedvolatiles contain cannabinoids including cannabidiol and/ortetrahydrocannabinol, wherein the cannabidiol content ranges from0.00001 weight percent to 25 weight percent and the tetrahydrocannabinolcontent ranges from 4 weight percent to 66 weight percent.

In embodiments, cannabinoids are obtained from the leaves, buds, stems,and/or volatiles, of cannabis or DANLEO III. In embodiments, thecannabinoids are extracted with a heated solvent and the resultingaqueous extract is passed through an adsorption resin to trap andconcentrate cannabinoids. Generally, the resin can be desorbed bywashing the resin with organic solvents like methanol or ethanol torelease the cannabinoids. Typically, the cannabinoid product isrecrystallized with a solvent such as methanol or ethanol. Typically,the cannabinoid product is recrystallized with a solvent such asmethanol. Ion-exchange resins have been used in the purificationprocess. In embodiments, the final product is typically spray-dried asshown in FIG. 17E′. In embodiments, the final product is evaporated asshown in FIG. 17D′.

As described herein, this disclosure provides for methods ofsupercritical fluid extraction and evaporator methods includingevaporation, rotary evaporation, vacuum evaporation, distillation,crystallization, vacuum flashing, wiped film evaporation,emulsification, filtration, and spray drying. Methods for the recoveryof terpenes and/or cannabidiol and/or tetrahydrocannabinol from cannabisusing supercritical CO2, filtration technology, and water or organicsolvents, such as methanol and ethanol, may also be used.

FIG. 17H′ shows one non-limiting embodiment of a continuous cannabinoidextraction process. In embodiments, the cannabis (HAA) can be introducedto an extraction vessel (HAI). In embodiments, the cannabis (HAA)includes pieces or portions of harvested cannabis, trimmed cannabis,dried cannabis, wet cannabis, heated cannabis, or solvent extractedcannabis. In embodiments, the cannabis (HAA) can first introduced to awater removal system (HZB) to reduce its moisture content. Inembodiments, the water removal system (HZB) is a dryer (HZC). Inembodiments, the dryer (HZC) includes a drum dryer, a vacuum dryer,rotary dryer, steam tube dryer, indirect dryer, direct dryer,indirectly-fired dryer, directly-fired dryer, tray dryer, tunnel dryer,roller dryers, pneumatic dryer, trough dryer, bin dryer, belt dryer,freeze dryer, or a microwave using microwave radiation and/or variablefrequency microwave radiation. In embodiments, the dryer (HZC) includesan indirectly-fired dryer or a directly-fired dryer that is fired with afuel, such as natural gas, propane, gasoline, fuel oil, oil, gaseousfuel, hydrocarbon, and liquid fuel.

In embodiments, water is removed from the cannabis (HAA) with microwaveradiation. In embodiments, the dryer (HZC) is a microwave. Inembodiments, the dryer (HZC) is a variable frequency microwave. Inembodiments, the microwave radiation is in the form of variablefrequency microwave radiation. In embodiments, the variable frequencymicrowave radiation operates at a frequency between about 2 GHz to about8 GHz. In embodiments, the variable frequency microwave radiationoperates at a frequency of about 2.45 GHz. In embodiments, the variablefrequency microwave radiation operates at a frequency selected from oneor more from the group consisting of 2 GHz to 2.15 Ghz, 2.15 GHz to 2.25Ghz, 2.25 GHz to 2.35 Ghz, 2.35 GHz to 2.45 Ghz, 2.45 GHz to 2.55 Ghz,2.55 GHz to 2.65 Ghz, 2.65 GHz to 2.75 Ghz, 2.75 GHz to 2.85 Ghz, 2.85GHz to 2.95 Ghz, 2.95 GHz to 3.05 Ghz, 3.05 GHz to 3.15 Ghz, 3.15 GHz to3.25 Ghz, 3.25 GHz to 3.35 Ghz, 3.35 GHz to 3.45 Ghz, 3.45 GHz to 3.55Ghz, 3.55 GHz to 3.65 Ghz, 3.65 GHz to 3.75 Ghz, 3.75 GHz to 3.85 Ghz,3.85 GHz to 3.95 Ghz, 3.95 GHz to 4.05 Ghz, 4.05 GHz to 4.15 Ghz, 4.15GHz to 4.25 Ghz, 4.25 GHz to 4.35 Ghz, 4.35 GHz to 4.45 Ghz, 4.45 GHz to4.55 Ghz, 4.55 GHz to 4.65 Ghz, 4.65 GHz to 4.75 Ghz, 4.75 GHz to 4.85Ghz, 4.85 GHz to 4.95 Ghz, 4.95 GHz to 5.05 Ghz, 5.05 GHz to 5.15 Ghz,5.15 GHz to 5.25 Ghz, 5.25 GHz to 5.35 Ghz, 5.35 GHz to 5.45 Ghz, 5.45GHz to 5.55 Ghz, 5.55 GHz to 5.65 Ghz, 5.65 GHz to 5.75 Ghz, 5.75 GHz to5.85 Ghz, 5.85 GHz to 5.95 Ghz, 5.95 GHz to 6.05 Ghz, 6.05 GHz to 6.15Ghz, 6.15 GHz to 6.25 Ghz, 6.25 GHz to 6.35 Ghz, 6.35 GHz to 6.45 Ghz,6.45 GHz to 6.55 Ghz, 6.55 GHz to 6.65 Ghz, 6.65 GHz to 6.75 Ghz, 6.75GHz to 6.85 Ghz, 6.85 GHz to 6.95 Ghz, 6.95 GHz to 7.05 Ghz, 7.05 GHz to7.15 Ghz, 7.15 GHz to 7.25 Ghz, 7.25 GHz to 7.35 Ghz, 7.35 GHz to 7.45Ghz, 7.45 GHz to 7.55 Ghz, 7.55 GHz to 7.65 Ghz, 7.65 GHz to 7.75 Ghz,7.75 GHz to 7.85 Ghz, 7.85 GHz to 7.95 Ghz, and 7.95 GHz to 8.00 Ghz.

In embodiments, the microwave has a power output that is measured inkilowatts (kW), the power output for the microwave operates at one ormore selected from the group of power ranges consisting of 10 kw to 20kw, 20 kw to 30 kw, 30 kw to 40 kw, 40 kw to 50 kw, 50 kw to 60 kw, 60kw to 70 kw, 70 kw to 80 kw, 80 kw to 90 kw, 90 kw to 100 kw, 100 kw to110 kw, 110 kw to 120 kw, 120 kw to 130 kw, 130 kw to 140 kw, 140 kw to150 kw, 150 kw to 160 kw, 160 kw to 170 kw, 170 kw to 180 kw, 180 kw to190 kw, 190 kw to 200 kw, 200 kw to 210 kw, 210 kw to 220 kw, 220 kw to230 kw, 230 kw to 240 kw, and 240 kw to 250 kw.

In embodiments, the microwave has a current that is measured in amps,the current for the microwave operates at one or more selected from thegroup of amp ranges consisting of 10 amps to 20 amps, 20 amps to 30amps, 30 amps to 40 amps, 40 amps to 50 amps, 50 amps to 60 amps, 60amps to 70 amps, 70 amps to 80 amps, 80 amps to 90 amps, 90 amps to 100amps, 100 amps to 110 amps, 110 amps to 120 amps, 120 amps to 130 amps,130 amps to 140 amps, 140 amps to 150 amps, 150 amps to 160 amps, 160amps to 170 amps, 170 amps to 180 amps, 180 amps to 190 amps, 190 ampsto 200 amps, 200 amps to 210 amps, 210 amps to 220 amps, 220 amps to 230amps, 230 amps to 240 amps, 240 amps to 250 amps, 250 amps to 260 amps,260 amps to 270 amps, 270 amps to 280 amps, 280 amps to 290 amps, and290 amps to 300 amps.

In embodiments, water is removed from the cannabis (HAA) over a durationof time between about 0.1 seconds to about 500 seconds. In embodiments,water is removed from the cannabis (HAA) over a duration of time betweenabout 0.05 minutes to 0.1 minutes, 0.1 minutes to 0.5 minutes, 0.5minutes to 1 minutes, 1 minute to 15 minutes, 15 minute to 30 minutes,30 minute to 60 minutes, 60 minute to 2 hours, 2 hours to 3 hours, 3hours to 4 hours, 4 hours to 5 hours, 5 hours to 6 hours, 6 hours to 7hours, 7 hours to 8 hours, 8 hours to 9 hours, 9 hours to 10 hours, 10hours to 11 hours, 11 hours to 12 hours, 12 hours to 13 hours, 13 hoursto 14 hours, 14 hours to 15 hours, 15 hours to 16 hours, 16 hours to 17hours, 17 hours to 18 hours, 18 hours to 19 hours, 19 hours to 20 hours,20 hours to 24 hours, 24 hours to 1 day, 1 day to 2 days, 2 days to 3days, 3 days to 4 days, 4 days to 5 days, 5 days to 6 days, 6 days to 7days, 7 days to 8 days, 8 days to 9 days, 9 days to 10 days, or 10 daysto 20 days.

In embodiments, the dryer (HZC) is a vacuum dryer that operates at apressure that is selected from one of more from the group consisting of:between about 0.001 inches of water to about 0.002 inches of water;between about 0.002 inches of water to about 0.003 inches of water;between about 0.003 inches of water to about 0.006 inches of water;between about 0.006 inches of water to about 0.012 inches of water;between about 0.012 inches of water to about 0.024 inches of water;between about 0.024 inches of water to about 0.050 inches of water;between about 0.050 inches of water to about 0.075 inches of water;between about 0.075 inches of water to about 0.150 inches of water;between about 0.150 inches of water to about 0.300 inches of water;between about 0.300 inches of water to about 0.450 inches of water;between about 0.450 inches of water to about 0.473 inches of water;between about 0.473 inches of water to about 0.496 inches of water;between about 0.496 inches of water to about 0.521 inches of water;between about 0.521 inches of water to about 0.547 inches of water;between about 0.547 inches of water to about 0.574 inches of water;between about 0.574 inches of water to about 0.603 inches of water;between about 0.603 inches of water to about 0.633 inches of water;between about 0.633 inches of water to about 0.665 inches of water;between about 0.665 inches of water to about 0.698 inches of water;between about 0.698 inches of water to about 0.733 inches of water;between about 0.733 inches of water to about 0.770 inches of water;between about 0.770 inches of water to about 0.808 inches of water;between about 0.808 inches of water to about 0.849 inches of water;between about 0.849 inches of water to about 0.891 inches of water;between about 0.891 inches of water to about 0.936 inches of water;between about 0.936 inches of water to about 0.982 inches of water;between about 0.982 inches of water to about 1.031 inches of water;between about 1.031 inches of water to about 1.083 inches of water;between about 1.083 inches of water to about 1.137 inches of water;between about 1.137 inches of water to about 1.194 inches of water;between about 1.194 inches of water to about 1.254 inches of water;between about 1.254 inches of water to about 1.316 inches of water;between about 1.316 inches of water to about 1.382 inches of water;between about 1.382 inches of water to about 1.451 inches of water;between about 1.451 inches of water to about 1.524 inches of water;between about 1.524 inches of water to about 2.286 inches of water;between about 2.286 inches of water to about 3.429 inches of water;between about 3.429 inches of water to about 5.143 inches of water;between about 5.143 inches of water to about 7.715 inches of water;between about 7.715 inches of water to about 11.572 inches of water;between about 11.572 inches of water to about 17.358 inches of water;between about 17.358 inches of water to about 26.037 inches of water;between about 26.037 inches of water to about 39.055 inches of water;between about 39.055 inches of water to about 58.582 inches of water;between about 58.582 inches of water to about 87.873 inches of water;between about 87.873 inches of water to about 131.810 inches of water;between about 131.810 inches of water to about 197.715 inches of water;between about 197.715 inches of water to about 296.573 inches of water;or, between about 296.573 inches of water to about 400 inches of water.

In embodiments, the dryer (HZC) can be operated by electricity, fluegas, solar power from at least one solar panel (SOLAR′), a fuel cell, ora combustion stream (LEM, LFD) as shown in FIG. 17F′. The dryer (HZC)can reduce the moisture of the cannabis (HAA) with a gas (HZA). Inembodiments, the gas (HZA) includes an oxygen-containing gas whichincludes air, oxygen-enriched-air i.e. greater than 21 mole % O₂, andsubstantially pure oxygen, i.e. greater than about 95 mole % oxygen (theremainder usually comprising N₂ and rare gases). In embodiments, the gas(HZA) may include flue gas which includes a vapor or gaseous mixturecontaining varying amounts of nitrogen (N₂), carbon dioxide (CO₂), water(H₂O), and oxygen (O₂). Flue gas is generated from the thermochemicalprocess of combustion. In embodiments, the gas (HZA) may include acombustion stream.

In embodiments, a water-depleted cannabis (HZE) or a dried cannabis(HZE′) is discharged from the water removal system (HZB) and has amoisture content (measured in weight percent of water) that is selectedfrom one of more from the group consisting of: between about between0.25 to 0.5, 0.5 to 1, 1 to 3, 3 to 5, 5 to 7, 7 to 9, 9 to 11, 11 to13, or 13 to 15.

A moisture content of the water-depleted cannabis (HZE) or a driedcannabis (HZE′) may be measured with a moisture sensor (HZD). Inembodiments, the moisture sensor (HZD) is selected from one or more fromthe group consisting of a halogen moisture sensor, mass spectrometer,Fourier transform infrared spectroscopy, infrared spectroscopy, radiofrequency (RF), a DC resistance circuit, frequency domain reflectometry(FDR), time domain reflectometry (TDR), time domain transmissometry(TDT), oven drying, gravimetric testing, forced air oven, vacuum oven,microwave, variable frequency microwave radiation, IR drying, toluenedistillation, Karl Fischer titration, or any conceivable instantaneouscontact or non-contact moisture analyzer. In embodiments, time-domainreflectometry or TDR is a measurement technique used to determine thecharacteristics of cannabis (HAA) by observing reflected waveforms. Inembodiments, time-domain transmissometry (TDT) is an analogous techniquethat measures the transmitted (rather than reflected) impulse ofcannabis (HAA).

In embodiments, the moisture sensor (HZD) is configured to input asignal to the computer. In embodiments, the moisture content of thewater-depleted cannabis (HZE) may be obtained through thermo-gravimetryor the loss-on-drying principle. In embodiments, the moisture sensor(HZD) includes a mass sensor and a heat source. The starting weight isrecorded by the mass sensor. The heat source applies heat to thecannabis (HAA). The ending weight of the water-depleted cannabis (HZE)or a dried cannabis (HZE′) is then recorded via the mass sensor. Thetotal loss in mass (the difference in mass of the water-depletedcannabis (HZE) and the cannabis (HAA)) is used to obtain the moisturecontent.

In embodiments, the cannabis (HAA′) includes harvested cannabis, trimmedcannabis, dried cannabis, wet cannabis, heated cannabis, carbon dioxideextracted cannabidiol and/or tetrahydrocannabinol, extractedcannabidiol, cannabidiol, carbon dioxide extracted cannabidiol,terpenes, carbon dioxide extracted terpenes, and/or extracted terpenes.The cannabis (HAA, HAA′) may come from any number of drawings disclosedwithin this specification and the cannabis (HAA′) can be grown in anynumber of ways.

A first cannabis sensor (HAC) is provided to measure the pressure,temperature, moisture, purity, pH, electrical conductivity, or elementalmake-up of the cannabis (HAA′). A first cannabis flow valve (HAE) isprovided to determine the content of cannabis (HAA′) that is introduceddownstream to the extraction vessel (HAI). A second cannabis sensor(HAC) is provided to measure the pressure, temperature, moisture,purity, pH, electrical conductivity, or elemental make-up of thecannabis (HAA′) to the extraction vessel (HAI).

A solvent (HAB, HAB′) is made available to the extraction vessel (HAI).The extraction vessel (HAI) is configured to accept a cannabis (HAA,HAA′) and a solvent (HAB, HAB′). In embodiments, the solvent (HAB)includes water, ethanol, an alcohol, an alcohol mixture, deionizedwater, treated water, filtered water. In embodiments, the solvent (HAB′)is pressurized and comes from a solvent treatment system (H-WTS) whichmay or may not treat solvent (such as water) that was passed on from asolvent recovery system. In embodiments, the solvent recovery systemincludes evaporation. In embodiments, the solvent recovery systemincludes distillation.

In embodiments, the solvent (HAB) includes a non-polar solvent selectedfrom one or more of the group consisting of pentane, petroleum ether,hexanes, n-hexane, heptane, diisopropyl ether, toluene, chloroform, andmethylene chloride; preferably petroleum ether, hexanes, n-hexane,heptane, and n-heptane.

In embodiments, the solvent (HAB) includes a non-polar solvent selectedfrom one or more of the group consisting of pentane, petroleum ether,hexanes, n-hexane, n-heptane, heptanes, diisopropyl ether, toluene,chloroform, and methylene chloride. In embodiments, the first solvent Ain the binary solvent system is petroleum ether, a heptane, orn-heptane.

A first solvent sensor (HAD) is provided to measure the pressure,temperature, moisture, purity, pH, electrical conductivity, or elementalmake-up of the solvent (HAB). A first solvent flow valve (HAF) isprovided to determine the content of solvent (HAB) that is introduceddownstream to the extraction vessel (HAI). A second solvent sensor (HAH)is provided to measure the pressure, temperature, moisture, purity, pH,electrical conductivity, or elemental make-up of the solvent (HAB) tothe extraction vessel (HAI). In embodiments, insects are mixed withcannabis (HAA, HAA′) prior to the extraction vessel (HAI).

In embodiments, the extraction vessel (HAI) is provided to accept atleast a portion of the cannabis (HAA, HAA′). A solvent (HAB, HAB′) ismade available to the extraction vessel (HAI). The extraction vessel(HAI) is configured to accept a cannabis (HAA, HAA′) and a solvent (HAB,HAB′). In embodiments, the extraction vessel (HAI) has an interior(HAJ). In embodiments, the interior (HAJ) of the extraction vessel (HAI)is the extraction zone (HAI′) where cannabinoids are extracted from thecannabis (HAA, HAA′) by use a solvent (HAB, HAB′).

In embodiments, the extraction vessel (HAI) is a continuously stirredtank reactor having a jacketed reactor equipped with a steam supplysystem and at least one steam trap. In embodiments, the extractionvessel (HAI) is equipped with a level sensor (HAL) that is configured toinput a signal (HAK) to the computer (COMP). In embodiments, theextraction vessel (HAI) is equipped with a pH sensor (HAL′) that isconfigured to input a signal (HAK′) to the computer (COMP). Inembodiments, the extraction vessel (HAI) is equipped with an auger (HA1)that has a motor (HA2). The motor (HA2) of the auger (HA1) rotates theauger (HA1) to mix the contents within the interior (HAJ) of theextraction vessel (HAI). In embodiments, the extraction vessel (HAI) isequipped with a temperature sensor (HA3) that is configured to input asignal (HA4) to the computer (COMP). In embodiments, the extractionvessel (HAI) is equipped with a heat exchanger (HAM) to heat and/or coolthe contents within the interior (HAJ) of the extraction vessel (HAI).In embodiments, the extraction vessel (HAI) outputs a crude cannabinoidextract (HAN).

In embodiments, the crude cannabinoids are admixed with water or asolvent to provide a crude extract stream which comprises from one ormore from the group consisting of 1 weight percent to 5 weight percent,5 weight percent to 10 weight percent, 10 weight percent to 15 weightpercent, 15 weight percent to 20 weight percent, 20 weight percent to 25weight percent, 25 weight percent to 30 weight percent, 30 weightpercent to 35 weight percent, 35 weight percent to 40 weight percent, 40weight percent to 45 weight percent, 45 weight percent to 50 weightpercent, 50 weight percent to 55 weight percent, 55 weight percent to 60weight percent, 60 weight percent to 65 weight percent, 65 weightpercent to 70 weight percent, 70 weight percent to 75 weight percent, 75weight percent to 80 weight percent, 80 weight percent to 85 weightpercent, 85 weight percent to 90 weight percent, and 90 to 100 weightpercent.

Following the extraction of the cannabinoids (such as CBD, THC) fromleaves, buds, stems, and/or volatiles, of cannabis or DANLEO III, anextract stream comprising crude cannabinoids is withdrawn from theextraction zone (HAI′). In embodiments, the crude cannabinoids areadmixed with water or a solvent to provide a crude cannabinoid extract(HAN).

In embodiments, the crude cannabinoid extract (HAN) discharged from theextraction vessel (HAI) is made available to a crude cannabinoid extractpump (HAO). In embodiments, the crude cannabinoid extract pump (HAO)pressurizes and pumps the crude cannabinoid extract (HAN) to form apressurized crude cannabinoid extract (HAX, HAX′). In embodiments, thecrude cannabinoid extract pump (HAO) is equipped with a motor (HAP) anda controller (HAQ) that is configured to input and/or output a signal(HAR) to the computer (COMP). A valve (HAU) may be provided to regulatethe flow of the pressurized crude cannabinoid extract (HAX, HAX′). Inembodiments, the valve (HAU) is equipped with a controller (HAV) that isconfigured to input and/or output a signal (HAW) to the computer (COMP).In embodiments, a pressure sensor (HAS) is provided to measure thepressure of the pressurized crude cannabinoid extract (HAX, HAX′) thatis discharged from the crude cannabinoid extract pump (HAO). Inembodiments, the pressure sensor (HAS) inputs a signal (HAT) to thecomputer (COMP).

In embodiments, the crude cannabinoid extract pump (HAO) pressurizes thecrude cannabinoid extract (HAN) to form a pressurized crude cannabinoidextract (HAX, HAX′) at a pressure that includes one or more pressureranges selected from the group consisting of 10 pounds per square inch(PSI) to 20 PSI, 20 PSI to 40 PSI, 40 PSI to 60 PSI, 60 PSI to 80 PSI,80 PSI to 100 PSI, 100 PSI to 125 PSI, 125 PSI to 150 PSI, 150 PSI to175 PSI, 175 PSI to 200 PSI, 200 PSI to 225 PSI, 225 PSI to 250 PSI, 250PSI to 275 PSI, 275 PSI to 300 PSI, 300 PSI to 325 PSI, 325 PSI to 350PSI, 350 PSI to 375 PSI, 375 PSI to 400 PSI, 400 PSI to 425 PSI, 425 PSIto 450 PSI, 450 PSI to 475 PSI, and 475 PSI to 500 PSI. In embodiments,the crude cannabinoid extract pump (HAO) pressurizes the crudecannabinoid extract (HAN) to form a pressurized crude cannabinoidextract (HAX, HAX′) which is then introduced to a heat exchanger (HAY).In embodiments, the heat exchanger (HAY) is provided with a heattransfer medium (HAZ) to heat or cool the pressurized crude cannabinoidextract (HAX, HAX′).

In embodiments, at least a portion of the pressurized crude cannabinoidextract (HAX′) is recycled back to the interior (HAJ) of the extractionvessel (HAI) via a bypass (HBB). A crude cannabinoid extract valve (HBA)is positioned on the bypass (HBB) to permit recycled pressurized crudecannabinoid extract (HAX′) to flow back into the interior (HAJ) of theextraction vessel (HAI).

In embodiments, at least a portion of the pressurized crude cannabinoidextract (HAX) is introduced to a first filter (HBC) and a second filter(HBF). In embodiments, the first filter (HBC) has an interior (HBD) andat least one filter element (HBE). In embodiments, the second filter(HBF) has an interior (HBG) and at least one filter element (HBH). Inembodiments, the first filtered crude cannabinoid extract (HBI′) isdischarged from the first filter (HBC) and a second filtered crudecannabinoid extract (HBI″) is discharged from the second filter (HBF).In embodiments, the first filtered crude cannabinoid extract (HBI′) andthe second filtered crude cannabinoid extract (HBI″) are combined toform a filtered crude cannabinoid extract (HBI) that has less solids init relative to the pressurized crude cannabinoid extract (HAX). Inembodiments, the first filter (HBC) and the second filter (HBF) alsodischarge solids (HBK) and solvent (HBJ). In embodiments, the solvent(HBJ) discharged from the first filter (HBC) and the second filter (HBF)is routed to the solvent treatment system (H-WTS) as discussed below.

In embodiments, the crude cannabinoid extract (HAN) is passed to thefilter (HBC, HBF) to remove any solid particles to provide a filteredcrude cannabinoid extract (HBI). In embodiments, the filtration iscarried at a microfiltration temperature ranging from one or more fromthe group consisting of 70 degrees F. to 100 degrees F., 100 deg F. to110 deg F., 110 deg F. to 120 deg F., 120 deg F. to 130 deg F., 130 degF. to 140 deg F., 140 deg F. to 150 deg F., 150 deg F. to 160 deg F.,160 deg F. to 170 deg F., 170 deg F. to 180 deg F., 180 deg F. to 190deg F., 190 deg F. to 200 deg F., 200 deg F. to 210 deg F., 210 deg F.to 212 deg F.

In embodiments, the filtration is carried out in a filter (HBC, HBF) hasa pore size that ranges from rom one or more from the group consistingof 0.03 microns to 0.05 microns, 0.05 microns to 0.07 microns, 0.07microns to 0.09 microns, 0.09 microns to 0.11 microns, 0.11 microns to0.13 microns, 0.13 microns to 0.15 microns, 0.15 microns to 0.17microns, 0.17 microns to 0.19 microns, 0.19 microns to 0.21 microns,0.21 microns to 0.23 microns, 0.23 microns to 0.25 microns, 0.25 micronsto 0.27 microns, 0.27 microns to 0.29 microns, 0.29 microns to 0.31microns, 0.31 microns to 0.33 microns, 0.33 microns to 0.35 microns,0.35 microns to 0.37 microns, 0.37 microns to 0.39 microns, 0.39 micronsto 0.41 microns, 0.41 microns to 0.43 microns, 0.43 microns to 0.45microns, 0.45 microns to 0.47 microns, 0.47 microns to 0.49 microns,0.49 microns to 0.51 microns, 0.51 microns to 0.61 microns, 0.61 micronsto 0.71 microns, 0.71 microns to 0.81 microns, 0.81 microns to 0.91microns, 0.91 microns to 1.01 microns, 1.01 microns to 1.5 microns, 1.5microns to 2 microns, 2 microns to 2.5 microns, 2.5 microns to 3microns, 3 microns to 3.5 microns, 3.5 microns to 4 microns, 4 micronsto 4.5 microns, 4.5 microns to 5 microns, 5 microns to 5.5 microns, 5.5microns to 6 microns, 6 microns to 6.5 microns, 6.5 microns to 7microns, 7 microns to 7.5 microns, 7.5 microns to 8 microns, 8 micronsto 8.5 microns, 8.5 microns to 9 microns, 9 microns to 9.5 microns, and9.5 microns to 10 microns, or at least 10 microns.

In embodiments, the filtration is carried out in a filter (HBC, HBF)that includes one or more filter types selected from the groupconsisting of a candle filter, a centrifuge cloth filter, filter presscloth filter, filter bag, vertical belt press cloth filter, basketfilter, rotary vacuum filter, rotary filter, drum filter, leaf filter,plate filter, batch filter, and a continuous filter.

In embodiments, any of the pumps in this patent specification have apump discharge velocity that is selected from one or more pump velocityranges consisting of: 0.65 feet per second to 0.75 feet per second, 0.75feet per second to 0.85 feet per second, 0.85 feet per second to 0.95feet per second, 0.95 feet per second to 1.05 feet per second, 1.05 feetper second to 1.15 feet per second, 1.15 feet per second to 1.25 feetper second, 1.25 feet per second to 1.35 feet per second, 1.35 feet persecond to 1.45 feet per second, 1.45 feet per second to 1.55 feet persecond, 1.55 feet per second to 1.65 feet per second, 1.65 feet persecond to 1.75 feet per second, 1.75 feet per second to 1.85 feet persecond, 1.85 feet per second to 1.95 feet per second, 1.95 feet persecond to 2.05 feet per second, 2.05 feet per second to 2.15 feet persecond, 2.15 feet per second to 2.25 feet per second, 2.25 feet persecond to 2.35 feet per second, 2.35 feet per second to 2.45 feet persecond, 2.45 feet per second to 2.55 feet per second, 2.55 feet persecond to 2.65 feet per second, 2.65 feet per second to 2.75 feet persecond, 2.75 feet per second to 2.85 feet per second, 2.85 feet persecond to 2.95 feet per second, 2.95 feet per second to 3.05 feet persecond, 3.05 feet per second to 3.15 feet per second, 3.15 feet persecond to 3.25 feet per second, 3.25 feet per second to 3.35 feet persecond, 3.35 feet per second to 3.45 feet per second, 3.45 feet persecond to 3.55 feet per second, 3.55 feet per second to 3.65 feet persecond, 3.65 feet per second to 3.75 feet per second, 3.75 feet persecond to 3.85 feet per second, 3.85 feet per second to 3.95 feet persecond, 3.95 feet per second to 4.05 feet per second, 4.05 feet persecond to 4.15 feet per second, 4.15 feet per second to 4.25 feet persecond, 4.25 feet per second to 4.35 feet per second, 4.35 feet persecond to 4.45 feet per second, 4.45 feet per second to 4.55 feet persecond, 4.55 feet per second to 4.65 feet per second, 4.65 feet persecond to 4.75 feet per second, 4.75 feet per second to 4.85 feet persecond, 4.85 feet per second to 4.90 feet per second, and 4.90 feet persecond to 5.00 feet per second. This is true especially for all pumps onFIGS. 1-18.

In embodiments, any of the pumps in this patent specification have apump discharge velocity that is selected from one or more pump velocityranges consisting of: 5.00 feet per second to 5.10 feet per second, 5.10feet per second to 5.20 feet per second, 5.20 feet per second to 5.30feet per second, 5.30 feet per second to 5.40 feet per second, 5.40 feetper second to 5.50 feet per second, 5.50 feet per second to 5.60 feetper second, 5.60 feet per second to 5.70 feet per second, 5.70 feet persecond to 5.80 feet per second, 5.80 feet per second to 5.90 feet persecond, 5.90 feet per second to 6.00 feet per second, 6.00 feet persecond to 6.10 feet per second, 6.10 feet per second to 6.20 feet persecond, 6.20 feet per second to 6.30 feet per second, 6.30 feet persecond to 6.40 feet per second, 6.40 feet per second to 6.50 feet persecond, 6.50 feet per second to 6.60 feet per second, 6.60 feet persecond to 6.70 feet per second, 6.70 feet per second to 6.80 feet persecond, 6.80 feet per second to 6.90 feet per second, 6.90 feet persecond to 7.00 feet per second, 7.00 feet per second to 7.10 feet persecond, 7.10 feet per second to 7.20 feet per second, 7.20 feet persecond to 7.30 feet per second, 7.30 feet per second to 7.40 feet persecond, 7.40 feet per second to 7.50 feet per second, 7.50 feet persecond to 7.60 feet per second, 7.60 feet per second to 7.70 feet persecond, 7.70 feet per second to 7.80 feet per second, 7.80 feet persecond to 7.90 feet per second, 7.90 feet per second to 8.00 feet persecond, 8.00 feet per second to 8.10 feet per second, 8.10 feet persecond to 8.20 feet per second, 8.20 feet per second to 8.30 feet persecond, 8.30 feet per second to 8.40 feet per second, 8.40 feet persecond to 8.50 feet per second, 8.50 feet per second to 8.60 feet persecond, 8.60 feet per second to 8.70 feet per second, 8.70 feet persecond to 8.80 feet per second, 8.80 feet per second to 8.90 feet persecond, 8.90 feet per second to 9.00 feet per second, 9.00 feet persecond to 9.10 feet per second, 9.10 feet per second to 9.20 feet persecond, 9.20 feet per second to 9.30 feet per second, 9.30 feet persecond to 9.40 feet per second, 9.40 feet per second to 9.50 feet persecond, 9.50 feet per second to 9.60 feet per second, 9.60 feet persecond to 9.70 feet per second, 9.70 feet per second to 9.80 feet persecond, 9.80 feet per second to 9.90 feet per second, 9.90 feet persecond to 10.00 feet per second, and 10.00 feet per second to 20.00 feetper second. This is true especially for all pumps on FIGS. 1-18.

In embodiments, the filter (HBC, HBF) is comprised of one or more fromthe group consisting of membrane, hollow, nanofiltration,microfiltration, microfilter, nanofilter, metal, ceramic, cloth,particulate filter, candle filter, ceramic fiber, filter cartridge,fiber, and mesh. In embodiments, the filter is configured to have a facevelocity during depressurization ranging from 0.5 feet per minute to 50feet per minute. In embodiments, the filter is configured to have a facevelocity during filtration ranging from: 5 feet per minute to 10 feetper minute, 10 feet per minute to 15 feet per minute, 15 feet per minuteto 20 feet per minute, 20 feet per minute to 25 feet per minute, 25 feetper minute to 30 feet per minute, 30 feet per minute to 35 feet perminute, 35 feet per minute to 40 feet per minute, 40 feet per minute to45 feet per minute, 45 feet per minute to 50 feet per minute, 50 feetper minute to 55 feet per minute, 55 feet per minute to 60 feet perminute, 60 feet per minute to 65 feet per minute, 65 feet per minute to70 feet per minute, 70 feet per minute to 75 feet per minute, 75 feetper minute to 80 feet per minute, 80 feet per minute to 85 feet perminute, 85 feet per minute to 90 feet per minute, 90 feet per minute to95 feet per minute, 95 feet per minute to 100 feet per minute, 100 feetper minute to 125 feet per minute, 125 feet per minute to 150 feet perminute, 150 feet per minute to 175 feet per minute, 175 feet per minuteto 200 feet per minute, 200 feet per minute to 225 feet per minute, 225feet per minute to 250 feet per minute, 250 feet per minute to 275 feetper minute, 275 feet per minute to 300 feet per minute, 300 feet perminute to 325 feet per minute, 325 feet per minute to 350 feet perminute, 350 feet per minute to 375 feet per minute, 375 feet per minuteto 400 feet per minute, 400 feet per minute to 425 feet per minute, 425feet per minute to 450 feet per minute, 450 feet per minute to 475 feetper minute, 475 feet per minute to 500 feet per minute, 500 feet perminute to 525 feet per minute, 525 feet per minute to 550 feet perminute, 550 feet per minute to 575 feet per minute, 575 feet per minuteto 600 feet per minute, 600 feet per minute to 625 feet per minute, 625feet per minute to 650 feet per minute, 650 feet per minute to 675 feetper minute, 675 feet per minute to 700 feet per minute, 700 feet perminute to 725 feet per minute, 725 feet per minute to 750 feet perminute, 750 feet per minute to 775 feet per minute, 775 feet per minuteto 800 feet per minute, 800 feet per minute to 825 feet per minute, 825feet per minute to 850 feet per minute, 850 feet per minute to 875 feetper minute, 875 feet per minute to 900 feet per minute, 900 feet perminute to 925 feet per minute, 925 feet per minute to 950 feet perminute, 950 feet per minute to 975 feet per minute, and 975 feet perminute to 1,000 feet per minute.

In embodiments, the crude cannabinoids are admixed with water or asolvent to provide a crude extract which comprises from one or more fromthe group consisting of 20.5 weight percent to 21 weight percent, 21weight percent to 21.5 weight percent, 21.5 weight percent to 22 weightpercent, 22 weight percent to 22.5 weight percent, 22.5 weight percentto 23 weight percent, 23 weight percent to 23.5 weight percent, 23.5weight percent to 24 weight percent, 24 weight percent to 24.5 weightpercent, 24.5 weight percent to 25 weight percent, 25 weight percent to25.5 weight percent, 25.5 weight percent to 26 weight percent, 26 weightpercent to 26.5 weight percent, 26.5 weight percent to 27 weightpercent, 27 weight percent to 27.5 weight percent, 27.5 weight percentto 28 weight percent, 28 weight percent to 28.5 weight percent, 28.5weight percent to 29 weight percent, 29 weight percent to 29.5 weightpercent, 29.5 weight percent to 30 weight percent, 30 weight percent to30.5 weight percent, 30.5 weight percent to 31 weight percent, 31 weightpercent to 31.5 weight percent, 31.5 weight percent to 32 weightpercent, 32 weight percent to 32.5 weight percent, 32.5 weight percentto 33 weight percent, 33 weight percent to 33.5 weight percent, 33.5weight percent to 34 weight percent, 34 weight percent to 34.5 weightpercent, 34.5 weight percent to 35 weight percent, 35 weight percent to35.5 weight percent, 35.5 weight percent to 36 weight percent, 36 weightpercent to 36.5 weight percent, 36.5 weight percent to 37 weightpercent, 37 weight percent to 37.5 weight percent, 37.5 weight percentto 38 weight percent, 38 weight percent to 38.5 weight percent, 38.5weight percent to 39 weight percent, 39 weight percent to 39.5 weightpercent, and 39.5 weight percent to 40 weight percent.

In embodiments, the concentration of solids within the crude cannabinoidextract is selected from one or more from the group consisting of: 6.500weight percent to 6.625 weight percent, 6.625 weight percent to 6.750weight percent, 6.750 weight percent to 6.875 weight percent, 6.875weight percent to 7.000 weight percent, 7.000 weight percent to 7.125weight percent, 7.125 weight percent to 7.250 weight percent, 7.250weight percent to 7.375 weight percent, 7.375 weight percent to 7.500weight percent, 7.500 weight percent to 7.625 weight percent, 7.625weight percent to 7.750 weight percent, 7.750 weight percent to 7.875weight percent, 7.875 weight percent to 8.000 weight percent, 8.000weight percent to 8.125 weight percent, 8.125 weight percent to 8.250weight percent, 8.250 weight percent to 8.375 weight percent, 8.375weight percent to 8.500 weight percent, 8.500 weight percent to 8.625weight percent, 8.625 weight percent to 8.750 weight percent, 8.750weight percent to 8.875 weight percent, 8.875 weight percent to 9.000weight percent, 9.000 weight percent to 9.125 weight percent, 9.125weight percent to 9.250 weight percent, 9.250 weight percent to 9.375weight percent, 9.375 weight percent to 9.500 weight percent, 9.500weight percent to 9.625 weight percent, 9.625 weight percent to 9.750weight percent, 9.750 weight percent to 9.875 weight percent, 9.875weight percent to 10.000 weight percent, 10.000 weight percent to 10.125weight percent, 10.125 weight percent to 10.250 weight percent, 10.250weight percent to 10.375 weight percent, 10.375 weight percent to 10.500weight percent, 10.500 weight percent to 10.625 weight percent, 10.625weight percent to 10.750 weight percent, 10.750 weight percent to 10.875weight percent, 10.875 weight percent to 11.000 weight percent, 11.000weight percent to 11.125 weight percent, 11.125 weight percent to 11.250weight percent, 11.250 weight percent to 11.375 weight percent, 11.375weight percent to 11.500 weight percent, 11.500 weight percent to 11.625weight percent, 11.625 weight percent to 11.750 weight percent, 11.750weight percent to 11.875 weight percent, 11.875 weight percent to 12.000weight percent, 12.000 weight percent to 12.125 weight percent, 12.125weight percent to 12.250 weight percent, 12.250 weight percent to 12.375weight percent, 12.375 weight percent to 12.500 weight percent, 12.500weight percent to 12.625 weight percent, 12.625 weight percent to 12.750weight percent, 12.750 weight percent to 12.875 weight percent, 12.875weight percent to 13.000 weight percent, 13.000 weight percent to 13.125weight percent, 13.125 weight percent to 13.250 weight percent, 13.250weight percent to 13.375 weight percent, 13.375 weight percent to 13.500weight percent, 13.500 weight percent to 13.625 weight percent, 13.625weight percent to 13.750 weight percent, 13.750 weight percent to 13.875weight percent, 13.875 weight percent to 14.000 weight percent, 14.000weight percent to 14.125 weight percent, 14.125 weight percent to 14.250weight percent, 14.250 weight percent to 14.375 weight percent, 14.375weight percent to 14.500 weight percent, 14.500 weight percent to 14.625weight percent, 14.625 weight percent to 14.750 weight percent, 14.750weight percent to 14.875 weight percent, 14.875 weight percent to 15.000weight percent, 15.000 weight percent to 15.125 weight percent, 15.125weight percent to 15.250 weight percent, 15.250 weight percent to 15.375weight percent, 15.375 weight percent to 15.500 weight percent, 15.500weight percent to 15.625 weight percent, 15.625 weight percent to 15.750weight percent, 15.750 weight percent to 15.875 weight percent, 15.875weight percent to 16.000 weight percent, 16.000 weight percent to 16.125weight percent, 16.125 weight percent to 16.250 weight percent, 16.250weight percent to 16.375 weight percent, 16.375 weight percent to 16.500weight percent, 16.500 weight percent to 16.625 weight percent, 16.625weight percent to 16.750 weight percent, 16.750 weight percent to 16.875weight percent, 16.875 weight percent to 17.000 weight percent, 17.000weight percent to 17.125 weight percent, 17.125 weight percent to 17.250weight percent, 17.250 weight percent to 17.375 weight percent, 17.375weight percent to 17.500 weight percent, 17.500 weight percent to 17.625weight percent, 17.625 weight percent to 17.750 weight percent, 17.750weight percent to 17.875 weight percent, 17.875 weight percent to 18.000weight percent, 8.000 weight percent to 18.125 weight percent, 18.125weight percent to 18.250 weight percent, 18.250 weight percent to 18.375weight percent, 18.375 weight percent to 18.500 weight percent, 18.500weight percent to 18.625 weight percent, 18.625 weight percent to 18.750weight percent, 18.750 weight percent to 18.875 weight percent, 18.875weight percent to 19.000 weight percent, 19.000 weight percent to 19.125weight percent, 19.125 weight percent to 19.250 weight percent, 19.250weight percent to 19.375 weight percent, 19.375 weight percent to 19.500weight percent, 19.500 weight percent to 19.625 weight percent, 19.625weight percent to 19.750 weight percent, 19.750 weight percent to 19.875weight percent, and 19.875 weight percent to 20.000 weight percent.

In embodiments, the filtered crude cannabinoid extract (HBI, HBI′, HBI″)is passed from the first filter (HBC) and/or the second filter (HBF) andinto a crude cannabinoid extract vessel (HCA). In embodiments, crudecannabinoid extract vessel (HCA) is configured to accept the filteredcrude cannabinoid extract (HBI, HBI′, HBI″).

In embodiments, the crude cannabinoid extract vessel (HCA) is acontinuously stirred tank reactor having a jacketed reactor equippedwith a steam supply system and at least one steam trap. In embodiments,the crude cannabinoid extract vessel (HCA) is equipped with a levelsensor (HCC) that is configured to input a signal (HCD) to the computer(COMP). In embodiments, the crude cannabinoid extract vessel (HCA) isequipped with a pH sensor (HCE) that is configured to input a signal(HCF) to the computer (COMP). In embodiments, the crude cannabinoidextract vessel (HCA) is equipped with an auger (HCG) that has a motor(HCH). The motor (HCH) of the auger (HCG) rotates the auger (HCG) to mixthe contents within the interior (HCB) of the crude cannabinoid extractvessel (HCA). In embodiments, the crude cannabinoid extract vessel (HCA)is equipped with a temperature sensor that is configured to input asignal to the computer (COMP). In embodiments, the crude cannabinoidextract vessel (HCA) is equipped with a heat exchanger (HCl) to heatand/or cool the contents within the interior (HCB) of the crudecannabinoid extract vessel (HCA). In embodiments, the crude cannabinoidextract vessel (HCA) outputs a filtered crude cannabinoid extract (HCK).

A filtered crude cannabinoid extract (HCK) is discharged from theinterior (HCB) of the crude cannabinoid extract vessel (HCA) and istransferred to a crude cannabinoid extract pump (HCO). The crudecannabinoid extract pump (HCO) is equipped with a motor (HCP) and acontroller (HCQ) that is configured to input and/or output a signal(HCR) to the computer (COMP). The crude cannabinoid extract pump (HCO)pumps and pressurizes the filtered crude cannabinoid extract (HCK) toform a filtered and pressurized crude cannabinoid extract (HCM). Inembodiments, the filtered and pressurized crude cannabinoid extract(HCM) is used as a backflush supply (HCN) to regenerate in-situ thefirst filter (HBC) and/or the second filter (HBF). In embodiments, afilter (HCJ) is provided to polish the filtered and pressurized crudecannabinoid extract (HCM) to remove any additional solids that arepresent. In embodiments, a pressure sensor (HCS) is provided to measurethe pressure of the filtered and pressurized crude cannabinoid extract(HCM). In embodiments, the pressure sensor (HCS) is configured to inputa signal (HCT) to the computer (COMP).

In embodiments, the crude cannabinoid extract pump (HCO) pressurizes thefiltered crude cannabinoid extract (HCK) to form a filtered andpressurized crude cannabinoid extract (HCM) at a pressure that includesone or more pressure ranges selected from the group consisting of 10pounds per square inch (PSI) to 20 PSI, 20 PSI to 40 PSI, 40 PSI to 60PSI, 60 PSI to 80 PSI, 80 PSI to 100 PSI, 100 PSI to 125 PSI, 125 PSI to150 PSI, 150 PSI to 175 PSI, 175 PSI to 200 PSI, 200 PSI to 225 PSI, 225PSI to 250 PSI, 250 PSI to 275 PSI, 275 PSI to 300 PSI, 300 PSI to 325PSI, 325 PSI to 350 PSI, 350 PSI to 375 PSI, 375 PSI to 400 PSI, 400 PSIto 425 PSI, 425 PSI to 450 PSI, 450 PSI to 475 PSI, and 475 PSI to 500PSI.

In embodiments, the filtered and pressurized crude cannabinoid extract(HCM) is transferred from the crude cannabinoid extract pump (HCO) andinto a first adsorber system (SMB1). In embodiments, the first adsorbersystem (SMB1) is configured to input a filtered and pressurized crudecannabinoid extract (HCM) and a first desorbent (HDC). In embodiments,the first adsorber system (SMB1) is configured to output a first extract(HDA) and a first raffinate (HDE). In embodiments, the first extract(HDA) can also be called a primary extract (HDB). In embodiments, thefirst adsorber system (SMB1) includes an adsorber or plurality ofadsorbers containing an adsorbent.

In embodiments, the first adsorber system (SMB1) includes a plurality ofadsorbers containing adsorbent is provided and may be called thestationary phase. In embodiments, the adsorbent positioned within theadsorber or plurality of adsorbers may be called the stationary phase.The bed of adsorbent that is contained within the adsorber does not moveso therefore it is stationary. The plurality of beds of adsorbent thatare contained within the plurality of adsorbers does not move sotherefore it is stationary. In embodiments, at least a portion ofcannabis is dissolved in a solvent (e.g.—the filtered and pressurizedcrude cannabinoid extract (HCM)) and may be called the mobile phase.

In embodiments, a first adsorber system (SMB1) operates as a simulatedmoving bed chromatography (SMB chromatography) which is a continuousprocess. This is implemented by arranging several preparative columnsconnected in series and periodically changing the valve setting so thata movement of the solid phase in the opposite direction of the flow ofthe liquid phase is simulated. In embodiments, the system iscontinuously fed with a feed mixture (e.g.—the filtered and pressurizedcrude cannabinoid extract (HCM)) comprising the compounds to beseparated and an eluent (e.g.—the first desorbent (HDC) which is aliquid, water, treated water, or a solvent) while a raffinate and anextract are continuously withdrawn from the system.

In embodiments, the first adsorber system (SMB1) periodically switchesthe feed, eluent, extract and raffinate ports in the same direction. Thebasic premise of a simulated moving bed adsorber system is that theinlet and outlet ports are switched periodically in the direction of thefluid flow. This simulates the countercurrent movement of the phase inthe process. Chromatography is a technique used to separate mixtures. Inembodiments, the mixture may include cannabinoids and a solvent. Inembodiments, the mixture may include a filtered and pressurized crudecannabinoid extract (HCM). In embodiments, the mixture may includecannabinoids from a first solvent and volatiles mixture (FSVM). Inembodiments, the mixture may include cannabinoids from a secondvolatiles and solvent mixture (SVSM).

In embodiments, cannabinoids (e.g.—tetrahydrocannabinol,Δ9-tetrahydrocannabinol Δ9-THC, Δ8-tetrahydrocannabinol Δ8-THC,cannabichromene CBC, cannabidiol CBD, cannabigerol CBG, cannabinidiolCBND, and/or cannabinol CBN) are dissolved in a liquid solvent. Themixture of cannabinoids and the solvent may be called the mobile phase.The mobile phase is passed through an adsorber containing an adsorbent,the adsorbent within the adsorber may be called a stationary phase. Inembodiments, a moving bed adsorber may be used in which the stationaryphase would then move.

The mixture of cannabinoids and solvent are introduced into the adsorberand various constituents of the mixture travel at different speeds,causing them to separate. The separation is based on differentialpartitioning between the mobile and stationary phases. More than oneadsorber may be used so there may be various stationary phases. Subtledifferences in each of the cannabinoids' partition coefficient result indifferential retention on the stationary phase and thus affect theseparation. For example, some cannabinoids are more hydrophilic thanothers and are mode readily soluble in a solvent such as lipids andalcohol. These compounds in turn have a relatively larger partitioncoefficient than the cannabinoids that are less hydrophilic.

In embodiments, a relatively less hydrophilic cannabinoid has a greaterpartition coefficient than a cannabinoid that is more hydrophilic. Inembodiments, a relatively more hydrophobic cannabinoid has a greaterpartition coefficient than a cannabinoid that is less hydrophilic. Inother embodiments, a relatively less hydrophilic cannabinoid has agreater partition coefficient than a cannabinoid that is morehydrophilic. In other embodiments, a relatively more hydrophiliccannabinoid has a lesser partition coefficient than a cannabinoid thatis lesser hydrophilic.

In embodiments, tetrahydrocannabinol has a partition coefficient of6.99. In embodiments, Δ9-tetrahydrocannabinol Δ9-THC has a partitioncoefficient of 6.99. In embodiments, cannabidiol has a partitioncoefficient of 5.79. In embodiments, tetrahydrocannabinol has apartition coefficient that is greater than cannabidiol. In embodiments,tetrahydrocannabinol is more hydrophobic than cannabidiol. Inembodiments, cannabidiol is more hydrophilic than tetrahydrocannabinol.

Since tetrahydrocannabinol has a partition coefficient that is greaterthan cannabidiol, it will stay in the bed longer than the cannabidiol.In embodiments, the tetrahydrocannabinol will stay in the adsorber bedlonger than the cannabidiol. In embodiments, the cannabidiol will stayin the adsorber bed longer than the tetrahydrocannabinol. Inembodiments, the tetrahydrocannabinol will elute before the cannabidiol.In embodiments, the cannabidiol will elute before thetetrahydrocannabinol.

In embodiments, the first, second, and/or third adsorber systems (SMB1,SMB2, SMB3), are simulated moving bed processing systems and are cyclicsteady state processes configured to obtain pure components(e.g.—concentrated volatiles, an emulsion, etc.) are production ratesthat include one or more selected from the group consisting of 0.0015tons per day to 0.003 tons per day, 0.003 tons per day to 0.0045 tonsper day, 0.0045 tons per day to 0.006 tons per day, 0.006 tons per dayto 0.0075 tons per day, 0.0075 tons per day to 0.009 tons per day, 0.009tons per day to 0.0105 tons per day, 0.0105 tons per day to 0.012 tonsper day, 0.012 tons per day to 0.0135 tons per day, 0.0135 tons per dayto 0.015 tons per day, 0.015 tons per day to 0.03 tons per day, 0.03tons per day to 0.033 tons per day, 0.033 tons per day to 0.036 tons perday, 0.036 tons per day to 0.039 tons per day, 0.039 tons per day to0.042 tons per day, 0.042 tons per day to 0.045 tons per day, 0.045 tonsper day to 0.048 tons per day, 0.048 tons per day to 0.051 tons per day,0.051 tons per day to 0.054 tons per day, 0.054 tons per day to 0.057tons per day, 0.057 tons per day to 0.06 tons per day, 0.06 tons per dayto 0.063 tons per day, 0.063 tons per day to 0.066 tons per day, 0.066tons per day to 0.132 tons per day, 0.132 tons per day to 0.198 tons perday, 0.198 tons per day to 0.264 tons per day, 0.264 tons per day to0.33 tons per day, 0.33 tons per day to 0.396 tons per day, 0.396 tonsper day to 0.462 tons per day, 0.462 tons per day to 0.528 tons per day,0.528 tons per day to 0.594 tons per day, 0.594 tons per day to 0.66tons per day, 0.66 tons per day to 0.726 tons per day, 0.726 tons perday to 0.792 tons per day, 0.792 tons per day to 1.584 tons per day,1.584 tons per day to 3.168 tons per day, 3.168 tons per day to 6.336tons per day, 6.336 tons per day to 12.672 tons per day, 12.672 tons perday to 25.344 tons per day, 25.344 tons per day to 50.688 tons per day,50.688 tons per day to 101.376 tons per day.

In embodiments, the extract is the more highly adsorbed component. Inembodiments, the more highly adsorbed components are cannabinoids (suchas tetrahydrocannabinol, Δ9-tetrahydrocannabinol Δ9-THC,Δ8-tetrahydrocannabinol Δ8-THC, cannabichromene CBC, cannabidiol CBD,cannabigerol CBG, cannabinidiol CBND, and/or cannabinol CBN). Inembodiments, the extract is desorbed with a desorbent to collect as thefinal product. Desorption may take place under pressure swingdesorption, thermal swing desorption, or passing a heated and/or cooleddesorbent liquid do desorb the extract from the adsorption sites withinthe adsorber. In embodiments, the desorption may take place underpressure swing desorption, thermal swing desorption, or passing a firstheated desorbent liquid then a second cooled desorbent liquid do desorbthe extract from the adsorption sites within the adsorber.

In embodiments, the raffinate includes poorly adsorbed components. Thepoorly adsorbed components adsorb less to the adsorption sites or theadsorbent within the adsorber or plurality of adsorbers in relation tothe highly adsorbed components. In embodiments, the raffinate includes aliquid, first solvent, second solvent, water, alcohol, lipid. Inembodiments, the raffinate includes a solvent, the solvent includes oneor more from the group consisting of acetone, alcohol, ethanol, hexane,insect lipids, isobutane, isopropanol, liquid carbon dioxide, liquid,naphtha, and water. In embodiments, a mixture of cannabinoids and asolvent are provided to the simulated bed adsorber system. Inembodiments, the cannabinoids are the extract and the solvent is theraffinate. In embodiments, the extract is more highly adsorbedcomponents. In embodiments, the more highly adsorbed components arecannabinoids.

In embodiments, the raffinate includes cannabinoids. In embodiments, theraffinate includes cannabidiol. In embodiments, the raffinate includesTHC. In embodiments, the raffinate includes a mixture of cannabinoidsand water. In embodiments, the raffinate includes a mixture ofcannabidiol and water. In embodiments, the raffinate includes a mixtureof THC and water. In embodiments, the raffinate includes a mixture ofcannabinoids and ethanol. In embodiments, the raffinate includes amixture of cannabidiol and ethanol. In embodiments, the raffinateincludes a mixture of THC and ethanol. In embodiments, the raffinateincludes a mixture of cannabinoids and ethanol and water. Inembodiments, the raffinate includes a mixture of cannabidiol and ethanoland water. In embodiments, the raffinate includes a mixture of THC andethanol and water. In embodiments, the raffinate includes a mixture ofcannabinoids and methanol. In embodiments, the raffinate includes amixture of cannabidiol and methanol. In embodiments, the raffinateincludes a mixture of THC and methanol.

In embodiments, the raffinate includes a mixture of cannabinoids andmethanol and water. In embodiments, the raffinate includes a mixture ofcannabidiol and methanol and water. In embodiments, the raffinateincludes a mixture of THC and methanol and water.

In embodiments, the raffinate includes cannabinoids and ethanol at acannabinoid-to-ethanol-raffinate-ratio selected from the groupconsisting of: 0.0001 pounds of cannabinoids to per pound of ethanol to0.0002 pounds of cannabinoids to per pound of ethanol, 0.0002 pounds ofcannabinoids to per pound of ethanol to 0.0004 pounds of cannabinoids toper pound of ethanol, 0.0004 pounds of cannabinoids to per pound ofethanol to 0.0008 pounds of cannabinoids to per pound of ethanol, 0.0008pounds of cannabinoids to per pound of ethanol to 0.0016 pounds ofcannabinoids to per pound of ethanol, 0.0016 pounds of cannabinoids toper pound of ethanol to 0.0032 pounds of cannabinoids to per pound ofethanol, 0.0032 pounds of cannabinoids to per pound of ethanol to 0.0064pounds of cannabinoids to per pound of ethanol, 0.0064 pounds ofcannabinoids to per pound of ethanol to 0.0128 pounds of cannabinoids toper pound of ethanol, 0.0128 pounds of cannabinoids to per pound ofethanol to 0.0256 pounds of cannabinoids to per pound of ethanol, 0.0256pounds of cannabinoids to per pound of ethanol to 0.0512 pounds ofcannabinoids to per pound of ethanol, 0.0512 pounds of cannabinoids toper pound of ethanol to 0.06 pounds of cannabinoids to per pound ofethanol, 0.06 pounds of cannabinoids to per pound of ethanol to 0.07pounds of cannabinoids to per pound of ethanol, 0.07 pounds ofcannabinoids to per pound of ethanol to 0.08 pounds of cannabinoids toper pound of ethanol, 0.08 pounds of cannabinoids to per pound ofethanol to 0.09 pounds of cannabinoids to per pound of ethanol, 0.09pounds of cannabinoids to per pound of ethanol to 0.1 pounds ofcannabinoids to per pound of ethanol, 0.1 pounds of cannabinoids to perpound of ethanol to 0.233 pounds of cannabinoids to per pound ofethanol, 0.233 pounds of cannabinoids to per pound of ethanol to 0.366pounds of cannabinoids to per pound of ethanol, 0.366 pounds ofcannabinoids to per pound of ethanol to 0.499 pounds of cannabinoids toper pound of ethanol, and 0.499 pounds of cannabinoids to per pound ofethanol to 0.632 pounds of cannabinoids to per pound of ethanol;wherein: the cannabinoid-to-ethanol-ratio is defined as the weightpercent of the raffinate mixture including the pounds of cannabinoidsdivided by the pounds of ethanol.

In embodiments, the raffinate includes cannabinoids and methanol at acannabinoid-to-methanol-raffinate-ratio selected from the groupconsisting of: 0.0001 pounds of cannabinoids to per pound of methanol to0.0002 pounds of cannabinoids to per pound of methanol, 0.0002 pounds ofcannabinoids to per pound of methanol to 0.0004 pounds of cannabinoidsto per pound of methanol, 0.0004 pounds of cannabinoids to per pound ofmethanol to 0.0008 pounds of cannabinoids to per pound of methanol,0.0008 pounds of cannabinoids to per pound of methanol to 0.0016 poundsof cannabinoids to per pound of methanol, 0.0016 pounds of cannabinoidsto per pound of methanol to 0.0032 pounds of cannabinoids to per poundof methanol, 0.0032 pounds of cannabinoids to per pound of methanol to0.0064 pounds of cannabinoids to per pound of methanol, 0.0064 pounds ofcannabinoids to per pound of methanol to 0.0128 pounds of cannabinoidsto per pound of methanol, 0.0128 pounds of cannabinoids to per pound ofmethanol to 0.0256 pounds of cannabinoids to per pound of methanol,0.0256 pounds of cannabinoids to per pound of methanol to 0.0512 poundsof cannabinoids to per pound of methanol, 0.0512 pounds of cannabinoidsto per pound of methanol to 0.06 pounds of cannabinoids to per pound ofmethanol, 0.06 pounds of cannabinoids to per pound of methanol to 0.07pounds of cannabinoids to per pound of methanol, 0.07 pounds ofcannabinoids to per pound of methanol to 0.08 pounds of cannabinoids toper pound of methanol, 0.08 pounds of cannabinoids to per pound ofmethanol to 0.09 pounds of cannabinoids to per pound of methanol, 0.09pounds of cannabinoids to per pound of methanol to 0.1 pounds ofcannabinoids to per pound of methanol, 0.1 pounds of cannabinoids to perpound of methanol to 0.233 pounds of cannabinoids to per pound ofmethanol, 0.233 pounds of cannabinoids to per pound of methanol to 0.366pounds of cannabinoids to per pound of methanol, 0.366 pounds ofcannabinoids to per pound of methanol to 0.499 pounds of cannabinoids toper pound of methanol, and 0.499 pounds of cannabinoids to per pound ofmethanol to 0.632 pounds of cannabinoids to per pound of methanol;wherein: the cannabinoid-to-methanol-ratio is defined as the weightpercent of the raffinate mixture including the pounds of cannabinoidsdivided by the pounds of methanol.

In embodiments, the raffinate includes cannabinoids and water at acannabinoid-to-water-raffinate-ratio selected from the group consistingof: 0.0001 pounds of cannabinoids to per pound of water to 0.0002 poundsof cannabinoids to per pound of water, 0.0002 pounds of cannabinoids toper pound of water to 0.0004 pounds of cannabinoids to per pound ofwater, 0.0004 pounds of cannabinoids to per pound of water to 0.0008pounds of cannabinoids to per pound of water, 0.0008 pounds ofcannabinoids to per pound of water to 0.0016 pounds of cannabinoids toper pound of water, 0.0016 pounds of cannabinoids to per pound of waterto 0.0032 pounds of cannabinoids to per pound of water, 0.0032 pounds ofcannabinoids to per pound of water to 0.0064 pounds of cannabinoids toper pound of water, 0.0064 pounds of cannabinoids to per pound of waterto 0.0128 pounds of cannabinoids to per pound of water, 0.0128 pounds ofcannabinoids to per pound of water to 0.0256 pounds of cannabinoids toper pound of water, 0.0256 pounds of cannabinoids to per pound of waterto 0.0512 pounds of cannabinoids to per pound of water, 0.0512 pounds ofcannabinoids to per pound of water to 0.06 pounds of cannabinoids to perpound of water, 0.06 pounds of cannabinoids to per pound of water to0.07 pounds of cannabinoids to per pound of water, 0.07 pounds ofcannabinoids to per pound of water to 0.08 pounds of cannabinoids to perpound of water, 0.08 pounds of cannabinoids to per pound of water to0.09 pounds of cannabinoids to per pound of water, 0.09 pounds ofcannabinoids to per pound of water to 0.1 pounds of cannabinoids to perpound of water, 0.1 pounds of cannabinoids to per pound of water to0.233 pounds of cannabinoids to per pound of water, 0.233 pounds ofcannabinoids to per pound of water to 0.366 pounds of cannabinoids toper pound of water, 0.366 pounds of cannabinoids to per pound of waterto 0.499 pounds of cannabinoids to per pound of water, and 0.499 poundsof cannabinoids to per pound of water to 0.632 pounds of cannabinoids toper pound of water; wherein: the cannabinoid-to-water-ratio is definedas the weight percent of the raffinate mixture including the pounds ofcannabinoids divided by the pounds of water.

In embodiments, the raffinate includes THC and ethanol at aTHC-to-ethanol-raffinate-ratio selected from the group consisting of:0.0001 pounds of THC to per pound of ethanol to 0.0002 pounds of THC toper pound of ethanol, 0.0002 pounds of THC to per pound of ethanol to0.0004 pounds of THC to per pound of ethanol, 0.0004 pounds of THC toper pound of ethanol to 0.0008 pounds of THC to per pound of ethanol,0.0008 pounds of THC to per pound of ethanol to 0.0016 pounds of THC toper pound of ethanol, 0.0016 pounds of THC to per pound of ethanol to0.0032 pounds of THC to per pound of ethanol, 0.0032 pounds of THC toper pound of ethanol to 0.0064 pounds of THC to per pound of ethanol,0.0064 pounds of THC to per pound of ethanol to 0.0128 pounds of THC toper pound of ethanol, 0.0128 pounds of THC to per pound of ethanol to0.0256 pounds of THC to per pound of ethanol, 0.0256 pounds of THC toper pound of ethanol to 0.0512 pounds of THC to per pound of ethanol,0.0512 pounds of THC to per pound of ethanol to 0.06 pounds of THC toper pound of ethanol, 0.06 pounds of THC to per pound of ethanol to 0.07pounds of THC to per pound of ethanol, 0.07 pounds of THC to per poundof ethanol to 0.08 pounds of THC to per pound of ethanol, 0.08 pounds ofTHC to per pound of ethanol to 0.09 pounds of THC to per pound ofethanol, 0.09 pounds of THC to per pound of ethanol to 0.1 pounds of THCto per pound of ethanol, 0.1 pounds of THC to per pound of ethanol to0.233 pounds of THC to per pound of ethanol, 0.233 pounds of THC to perpound of ethanol to 0.366 pounds of THC to per pound of ethanol, 0.366pounds of THC to per pound of ethanol to 0.499 pounds of THC to perpound of ethanol, and 0.499 pounds of THC to per pound of ethanol to0.632 pounds of THC to per pound of ethanol; wherein: theTHC-to-ethanol-ratio is defined as the weight percent of the raffinatemixture including the pounds of THC divided by the pounds of ethanol.

In embodiments, the raffinate includes THC and methanol at aTHC-to-methanol-raffinate-ratio selected from the group consisting of:0.0001 pounds of THC to per pound of methanol to 0.0002 pounds of THC toper pound of methanol, 0.0002 pounds of THC to per pound of methanol to0.0004 pounds of THC to per pound of methanol, 0.0004 pounds of THC toper pound of methanol to 0.0008 pounds of THC to per pound of methanol,0.0008 pounds of THC to per pound of methanol to 0.0016 pounds of THC toper pound of methanol, 0.0016 pounds of THC to per pound of methanol to0.0032 pounds of THC to per pound of methanol, 0.0032 pounds of THC toper pound of methanol to 0.0064 pounds of THC to per pound of methanol,0.0064 pounds of THC to per pound of methanol to 0.0128 pounds of THC toper pound of methanol, 0.0128 pounds of THC to per pound of methanol to0.0256 pounds of THC to per pound of methanol, 0.0256 pounds of THC toper pound of methanol to 0.0512 pounds of THC to per pound of methanol,0.0512 pounds of THC to per pound of methanol to 0.06 pounds of THC toper pound of methanol, 0.06 pounds of THC to per pound of methanol to0.07 pounds of THC to per pound of methanol, 0.07 pounds of THC to perpound of methanol to 0.08 pounds of THC to per pound of methanol, 0.08pounds of THC to per pound of methanol to 0.09 pounds of THC to perpound of methanol, 0.09 pounds of THC to per pound of methanol to 0.1pounds of THC to per pound of methanol, 0.1 pounds of THC to per poundof methanol to 0.233 pounds of THC to per pound of methanol, 0.233pounds of THC to per pound of methanol to 0.366 pounds of THC to perpound of methanol, 0.366 pounds of THC to per pound of methanol to 0.499pounds of THC to per pound of methanol, and 0.499 pounds of THC to perpound of methanol to 0.632 pounds of THC to per pound of methanol;wherein: the THC-to-methanol-ratio is defined as the weight percent ofthe raffinate mixture including the pounds of THC divided by the poundsof methanol.

In embodiments, the raffinate includes THC and water at aTHC-to-water-raffinate-ratio selected from the group consisting of:0.0001 pounds of THC to per pound of water to 0.0002 pounds of THC toper pound of water, 0.0002 pounds of THC to per pound of water to 0.0004pounds of THC to per pound of water, 0.0004 pounds of THC to per poundof water to 0.0008 pounds of THC to per pound of water, 0.0008 pounds ofTHC to per pound of water to 0.0016 pounds of THC to per pound of water,0.0016 pounds of THC to per pound of water to 0.0032 pounds of THC toper pound of water, 0.0032 pounds of THC to per pound of water to 0.0064pounds of THC to per pound of water, 0.0064 pounds of THC to per poundof water to 0.0128 pounds of THC to per pound of water, 0.0128 pounds ofTHC to per pound of water to 0.0256 pounds of THC to per pound of water,0.0256 pounds of THC to per pound of water to 0.0512 pounds of THC toper pound of water, 0.0512 pounds of THC to per pound of water to 0.06pounds of THC to per pound of water, 0.06 pounds of THC to per pound ofwater to 0.07 pounds of THC to per pound of water, 0.07 pounds of THC toper pound of water to 0.08 pounds of THC to per pound of water, 0.08pounds of THC to per pound of water to 0.09 pounds of THC to per poundof water, 0.09 pounds of THC to per pound of water to 0.1 pounds of THCto per pound of water, 0.1 pounds of THC to per pound of water to 0.233pounds of THC to per pound of water, 0.233 pounds of THC to per pound ofwater to 0.366 pounds of THC to per pound of water, 0.366 pounds of THCto per pound of water to 0.499 pounds of THC to per pound of water, and0.499 pounds of THC to per pound of water to 0.632 pounds of THC to perpound of water; wherein: the THC-to-water-ratio is defined as the weightpercent of the raffinate mixture including the pounds of THC divided bythe pounds of water.

In embodiments, the raffinate includes CBD and ethanol at aCBD-to-ethanol-raffinate-ratio selected from the group consisting of:0.0001 pounds of CBD to per pound of ethanol to 0.0002 pounds of CBD toper pound of ethanol, 0.0002 pounds of CBD to per pound of ethanol to0.0004 pounds of CBD to per pound of ethanol, 0.0004 pounds of CBD toper pound of ethanol to 0.0008 pounds of CBD to per pound of ethanol,0.0008 pounds of CBD to per pound of ethanol to 0.0016 pounds of CBD toper pound of ethanol, 0.0016 pounds of CBD to per pound of ethanol to0.0032 pounds of CBD to per pound of ethanol, 0.0032 pounds of CBD toper pound of ethanol to 0.0064 pounds of CBD to per pound of ethanol,0.0064 pounds of CBD to per pound of ethanol to 0.0128 pounds of CBD toper pound of ethanol, 0.0128 pounds of CBD to per pound of ethanol to0.0256 pounds of CBD to per pound of ethanol, 0.0256 pounds of CBD toper pound of ethanol to 0.0512 pounds of CBD to per pound of ethanol,0.0512 pounds of CBD to per pound of ethanol to 0.06 pounds of CBD toper pound of ethanol, 0.06 pounds of CBD to per pound of ethanol to 0.07pounds of CBD to per pound of ethanol, 0.07 pounds of CBD to per poundof ethanol to 0.08 pounds of CBD to per pound of ethanol, 0.08 pounds ofCBD to per pound of ethanol to 0.09 pounds of CBD to per pound ofethanol, 0.09 pounds of CBD to per pound of ethanol to 0.1 pounds of CBDto per pound of ethanol, 0.1 pounds of CBD to per pound of ethanol to0.233 pounds of CBD to per pound of ethanol, 0.233 pounds of CBD to perpound of ethanol to 0.366 pounds of CBD to per pound of ethanol, 0.366pounds of CBD to per pound of ethanol to 0.499 pounds of CBD to perpound of ethanol, and 0.499 pounds of CBD to per pound of ethanol to0.632 pounds of CBD to per pound of ethanol; wherein: theCBD-to-ethanol-ratio is defined as the weight percent of the raffinatemixture including the pounds of CBD divided by the pounds of ethanol.

In embodiments, the raffinate includes CBD and methanol at aCBD-to-methanol-raffinate-ratio selected from the group consisting of:0.0001 pounds of CBD to per pound of methanol to 0.0002 pounds of CBD toper pound of methanol, 0.0002 pounds of CBD to per pound of methanol to0.0004 pounds of CBD to per pound of methanol, 0.0004 pounds of CBD toper pound of methanol to 0.0008 pounds of CBD to per pound of methanol,0.0008 pounds of CBD to per pound of methanol to 0.0016 pounds of CBD toper pound of methanol, 0.0016 pounds of CBD to per pound of methanol to0.0032 pounds of CBD to per pound of methanol, 0.0032 pounds of CBD toper pound of methanol to 0.0064 pounds of CBD to per pound of methanol,0.0064 pounds of CBD to per pound of methanol to 0.0128 pounds of CBD toper pound of methanol, 0.0128 pounds of CBD to per pound of methanol to0.0256 pounds of CBD to per pound of methanol, 0.0256 pounds of CBD toper pound of methanol to 0.0512 pounds of CBD to per pound of methanol,0.0512 pounds of CBD to per pound of methanol to 0.06 pounds of CBD toper pound of methanol, 0.06 pounds of CBD to per pound of methanol to0.07 pounds of CBD to per pound of methanol, 0.07 pounds of CBD to perpound of methanol to 0.08 pounds of CBD to per pound of methanol, 0.08pounds of CBD to per pound of methanol to 0.09 pounds of CBD to perpound of methanol, 0.09 pounds of CBD to per pound of methanol to 0.1pounds of CBD to per pound of methanol, 0.1 pounds of CBD to per poundof methanol to 0.233 pounds of CBD to per pound of methanol, 0.233pounds of CBD to per pound of methanol to 0.366 pounds of CBD to perpound of methanol, 0.366 pounds of CBD to per pound of methanol to 0.499pounds of CBD to per pound of methanol, and 0.499 pounds of CBD to perpound of methanol to 0.632 pounds of CBD to per pound of methanol;wherein: the CBD-to-methanol-ratio is defined as the weight percent ofthe raffinate mixture including the pounds of CBD divided by the poundsof methanol.

In embodiments, the raffinate includes CBD and water at aCBD-to-water-raffinate-ratio selected from the group consisting of:0.0001 pounds of CBD to per pound of water to 0.0002 pounds of CBD toper pound of water, 0.0002 pounds of CBD to per pound of water to 0.0004pounds of CBD to per pound of water, 0.0004 pounds of CBD to per poundof water to 0.0008 pounds of CBD to per pound of water, 0.0008 pounds ofCBD to per pound of water to 0.0016 pounds of CBD to per pound of water,0.0016 pounds of CBD to per pound of water to 0.0032 pounds of CBD toper pound of water, 0.0032 pounds of CBD to per pound of water to 0.0064pounds of CBD to per pound of water, 0.0064 pounds of CBD to per poundof water to 0.0128 pounds of CBD to per pound of water, 0.0128 pounds ofCBD to per pound of water to 0.0256 pounds of CBD to per pound of water,0.0256 pounds of CBD to per pound of water to 0.0512 pounds of CBD toper pound of water, 0.0512 pounds of CBD to per pound of water to 0.06pounds of CBD to per pound of water, 0.06 pounds of CBD to per pound ofwater to 0.07 pounds of CBD to per pound of water, 0.07 pounds of CBD toper pound of water to 0.08 pounds of CBD to per pound of water, 0.08pounds of CBD to per pound of water to 0.09 pounds of CBD to per poundof water, 0.09 pounds of CBD to per pound of water to 0.1 pounds of CBDto per pound of water, 0.1 pounds of CBD to per pound of water to 0.233pounds of CBD to per pound of water, 0.233 pounds of CBD to per pound ofwater to 0.366 pounds of CBD to per pound of water, 0.366 pounds of CBDto per pound of water to 0.499 pounds of CBD to per pound of water, and0.499 pounds of CBD to per pound of water to 0.632 pounds of CBD to perpound of water; wherein: the CBD-to-water-ratio is defined as the weightpercent of the raffinate mixture including the pounds of CBD divided bythe pounds of water.

Desorbent (Eluent)

In embodiments, the eluent is the first desorbent (HDC). In embodiments,the eluent is in a supercritical state. In embodiments, the eluent isnot in a supercritical state. In embodiments, the eluent is a liquid. Inembodiments, the eluent can be an aqueous alcohol. In embodiments, theaqueous alcohol can comprise water and one or more short chain alcohols.In embodiments, the short chain alcohol can have from 1 to 6 carbonatoms. In embodiments, the examples of suitable alcohols includemethanol, ethanol, n-propanol, i-propanol, n-butanol, i-butanol,s-butanol and t-butanol. In some aspects of the present invention,methanol and ethanol can be used. In another aspect, methanol can beused. In embodiments, the eluent can be methyl tertiary butyl ether. Inembodiments, the eluent is a mixture of methanol, tetrahydrofuran, andwater. In embodiments, the eluent is water. In embodiments, the eluentis treated water. In embodiments, the eluent ranges from between 80 degF. to 90 deg F., 9 deg F. to 100 deg F., 100 deg F. to 110 deg F., 110deg F. to 120 deg F., 120 deg F. to 130 deg F., 130 deg F. to 140 degF., 140 deg F. to 150 deg F., 150 deg F. to 160 deg F., 160 deg F. to170 deg F., 170 deg F. to 180 deg F., 180 deg F. to 190 deg F., 190 degF. to 200 deg F., 200 deg F. to 210 deg F., 210 deg F. to 212 deg F.

In embodiments, the weight percent of ethanol in the eluent includes oneor more concentration ranges selected from the group consisting of: 15weight percent to 20 weight percent, 20 weight percent to 25 weightpercent, 25 weight percent to 30 weight percent, 30 weight percent to 35weight percent, 35 weight percent to 40 weight percent, 40 weightpercent to 45 weight percent, 45 weight percent to 50 weight percent, 50weight percent to 55 weight percent, 55 weight percent to 60 weightpercent, 60 weight percent to 65 weight percent, 65 weight percent to 70weight percent, 70 weight percent to 75 weight percent, 75 weightpercent to 80 weight percent, 80 weight percent to 85 weight percent, 85weight percent to 90 weight percent, 90 to 95 weight percent, 95 weightpercent to 99 weight percent, and 99 weight percent to 100 weightpercent, and 100 weight percent.

In embodiments, the weight percent of methanol in the eluent includesone or more concentration ranges selected from the group consisting of:15 weight percent to 20 weight percent, 20 weight percent to 25 weightpercent, 25 weight percent to 30 weight percent, 30 weight percent to 35weight percent, 35 weight percent to 40 weight percent, 40 weightpercent to 45 weight percent, 45 weight percent to 50 weight percent, 50weight percent to 55 weight percent, 55 weight percent to 60 weightpercent, 60 weight percent to 65 weight percent, 65 weight percent to 70weight percent, 70 weight percent to 75 weight percent, 75 weightpercent to 80 weight percent, 80 weight percent to 85 weight percent, 85weight percent to 90 weight percent, 90 to 95 weight percent, 95 weightpercent to 99 weight percent, and 99 weight percent to 100 weightpercent, and 100 weight percent.

In embodiments the weight percent of tetrahydrofuran in the eluentincludes one or more concentration ranges selected from the groupconsisting of: 0 weight percent to 1 weight percent, 1 weight percent to5 weight percent, 5 weight percent to 10 weight percent, 10 weightpercent to 15 weight percent, 15 weight percent to 20 weight percent, 20weight percent to 25 weight percent, 25 weight percent to 30 weightpercent, 30 weight percent to 35 weight percent, 35 weight percent to 40weight percent, 40 weight percent to 45 weight percent, 45 weightpercent to 50 weight percent, 50 weight percent to 55 weight percent, 55weight percent to 60 weight percent, 60 weight percent to 65 weightpercent, 65 weight percent to 70 weight percent, 70 weight percent to 75weight percent, 75 weight percent to 80 weight percent, 80 weightpercent to 85 weight percent, 85 weight percent to 90 weight percent, 90weight percent to 95 weight percent, 95 weight percent to 99 weightpercent, and 99 to 100 weight percent to percent, and 100 weightpercent.

In embodiments, the weight percent of water in the eluent includes oneor more concentration ranges selected from the group consisting of: 0weight percent to 1 weight percent, 1 weight percent to 5 weightpercent, 5 weight percent to 10 weight percent, 10 weight percent to 15weight percent, 15 weight percent to 20 weight percent, 20 weightpercent to 25 weight percent, 25 weight percent to 30 weight percent, 30weight percent to 35 weight percent, 35 weight percent to 40 weightpercent, 40 weight percent to 45 weight percent, 45 weight percent to 50weight percent, 50 weight percent to 55 weight percent, 55 weightpercent to 60 weight percent, 60 weight percent to 65 weight percent, 65weight percent to 70 weight percent, 70 weight percent to 75 weightpercent, 75 weight percent to 80 weight percent, 80 weight percent to 85weight percent, 85 weight percent to 90 weight percent, 90 weightpercent to 95 weight percent, 95 weight percent to 99 weight percent,and 99 weight percent to 100 weight percent, and 100 weight percent.

The process of the present invention relates to the purification ofterpenes and/or cannabidiol and/or tetrahydrocannabinol directly fromextracts of plant material in a process which uses novel chromatographicscheme. More specifically, Applicant has developed a sequence ofpurification steps and a novel simulated moving bed separation process(SMB) series of adsorbent/desorbent combinations and SMB configurationsto bring about the enrichment and purification of terpenes and/orcannabidiol and/or tetrahydrocannabinol, to provide a purified terpenesand/or cannabidiol and/or tetrahydrocannabinol product and without usingany potentially toxic organic solvent.

In embodiments, the adsorbent used in the simulated moving bed systememployed is a combination of styrene-divinyl benzene copolymer, ionexchange and hydrophobic interaction based stationary phase adsorbentsand a mobile phase comprising water in a combination of normal andreverse phase simulated moving bed separation zones to provide anenriched extract comprising major terpenes and/or cannabidiol and/ortetrahydrocannabinol.

In embodiments, the terpenes that are extracted from the SMB processhave a purity that includes one or more from the group consisting of 30percent purity to 40 percent purity, 40 percent purity to 50 percentpurity, 50 percent purity to 60 percent purity, 60 percent purity to 70percent purity, 70 percent purity to 80 percent purity, 80 percentpurity to 82 percent purity, 82 percent purity to 84 percent purity, 84percent purity to 86 percent purity, 86 percent purity to 88 percentpurity, 88 percent purity to 90 percent purity, 90 percent purity to 92percent purity, 92 percent purity to 92.5 percent purity, 92.5 percentpurity to 93 percent purity, 93 percent purity to 93.5 percent purity,93.5 percent purity to 94 percent purity, 94 percent purity to 94.5percent purity, 94.5 percent purity to 94.75 percent purity, 94.75percent purity to 95 percent purity, 95 percent purity to 95.25 percentpurity, 95.25 percent purity to 95.5 percent purity, 95.5 percent purityto 95.75 percent purity, 95.75 percent purity to 96 percent purity, 96percent purity to 96.25 percent purity, 96.25 percent purity to 96.5percent purity, 96.5 percent purity to 96.75 percent purity, 96.75percent purity to 97 percent purity, 97 percent purity to 97.25 percentpurity, 97.25 percent purity to 97.5 percent purity, 97.5 percent purityto 97.75 percent purity, 97.75 percent purity to 98 percent purity, 98percent purity to 98.25 percent purity, 98.25 percent purity to 98.5percent purity, 98.5 percent purity to 98.75 percent purity, 98.75percent purity to 99 percent purity, 99 percent purity to 99.25 percentpurity, 99.25 percent purity to 99.5 percent purity, 99.5 percent purityto 99.75 percent purity, and 99.75 percent purity to 100 percent purity.

In embodiments, the cannabidiol that are extracted from the SMB processhave a purity that includes one or more from the group consisting of 30percent purity to 40 percent purity, 40 percent purity to 50 percentpurity, 50 percent purity to 60 percent purity, 60 percent purity to 70percent purity, 70 percent purity to 80 percent purity, 80 percentpurity to 82 percent purity, 82 percent purity to 84 percent purity, 84percent purity to 86 percent purity, 86 percent purity to 88 percentpurity, 88 percent purity to 90 percent purity, 90 percent purity to 92percent purity, 92 percent purity to 92.5 percent purity, 92.5 percentpurity to 93 percent purity, 93 percent purity to 93.5 percent purity,93.5 percent purity to 94 percent purity, 94 percent purity to 94.5percent purity, 94.5 percent purity to 94.75 percent purity, 94.75percent purity to 95 percent purity, 95 percent purity to 95.25 percentpurity, 95.25 percent purity to 95.5 percent purity, 95.5 percent purityto 95.75 percent purity, 95.75 percent purity to 96 percent purity, 96percent purity to 96.25 percent purity, 96.25 percent purity to 96.5percent purity, 96.5 percent purity to 96.75 percent purity, 96.75percent purity to 97 percent purity, 97 percent purity to 97.25 percentpurity, 97.25 percent purity to 97.5 percent purity, 97.5 percent purityto 97.75 percent purity, 97.75 percent purity to 98 percent purity, 98percent purity to 98.25 percent purity, 98.25 percent purity to 98.5percent purity, 98.5 percent purity to 98.75 percent purity, 98.75percent purity to 99 percent purity, 99 percent purity to 99.25 percentpurity, 99.25 percent purity to 99.5 percent purity, 99.5 percent purityto 99.75 percent purity, and 99.75 percent purity to 100 percent purity.

In embodiments, the tetrahydrocannabinol that are extracted from the SMBprocess have a purity that includes one or more from the groupconsisting of 30 percent purity to 40 percent purity, 40 percent purityto 50 percent purity, 50 percent purity to 60 percent purity, 60 percentpurity to 70 percent purity, 70 percent purity to 80 percent purity, 80percent purity to 82 percent purity, 82 percent purity to 84 percentpurity, 84 percent purity to 86 percent purity, 86 percent purity to 88percent purity, 88 percent purity to 90 percent purity, 90 percentpurity to 92 percent purity, 92 percent purity to 92.5 percent purity,92.5 percent purity to 93 percent purity, 93 percent purity to 93.5percent purity, 93.5 percent purity to 94 percent purity, 94 percentpurity to 94.5 percent purity, 94.5 percent purity to 94.75 percentpurity, 94.75 percent purity to 95 percent purity, 95 percent purity to95.25 percent purity, 95.25 percent purity to 95.5 percent purity, 95.5percent purity to 95.75 percent purity, 95.75 percent purity to 96percent purity, 96 percent purity to 96.25 percent purity, 96.25 percentpurity to 96.5 percent purity, 96.5 percent purity to 96.75 percentpurity, 96.75 percent purity to 97 percent purity, 97 percent purity to97.25 percent purity, 97.25 percent purity to 97.5 percent purity, 97.5percent purity to 97.75 percent purity, 97.75 percent purity to 98percent purity, 98 percent purity to 98.25 percent purity, 98.25 percentpurity to 98.5 percent purity, 98.5 percent purity to 98.75 percentpurity, 98.75 percent purity to 99 percent purity, 99 percent purity to99.25 percent purity, 99.25 percent purity to 99.5 percent purity, 99.5percent purity to 99.75 percent purity, and 99.75 percent purity to 100percent purity.

In embodiments, the cannabinoids (Δ9-tetrahydrocannabinol Δ9-THC,Δ8-tetrahydrocannabinol Δ8-THC, cannabichromene CBC, cannabidiol CBD,cannabigerol CBG, cannabinidiol CBND, and/or cannabinol CBN,cannabidiol, tetrahydrocannabinol) that are extracted from the SMBprocess have a purity that includes one or more from the groupconsisting of 30 percent purity to 40 percent purity, 40 percent purityto 50 percent purity, 50 percent purity to 60 percent purity, 60 percentpurity to 70 percent purity, 70 percent purity to 80 percent purity, 80percent purity to 82 percent purity, 82 percent purity to 84 percentpurity, 84 percent purity to 86 percent purity, 86 percent purity to 88percent purity, 88 percent purity to 90 percent purity, 90 percentpurity to 92 percent purity, 92 percent purity to 92.5 percent purity,92.5 percent purity to 93 percent purity, 93 percent purity to 93.5percent purity, 93.5 percent purity to 94 percent purity, 94 percentpurity to 94.5 percent purity, 94.5 percent purity to 94.75 percentpurity, 94.75 percent purity to 95 percent purity, 95 percent purity to95.25 percent purity, 95.25 percent purity to 95.5 percent purity, 95.5percent purity to 95.75 percent purity, 95.75 percent purity to 96percent purity, 96 percent purity to 96.25 percent purity, 96.25 percentpurity to 96.5 percent purity, 96.5 percent purity to 96.75 percentpurity, 96.75 percent purity to 97 percent purity, 97 percent purity to97.25 percent purity, 97.25 percent purity to 97.5 percent purity, 97.5percent purity to 97.75 percent purity, 97.75 percent purity to 98percent purity, 98 percent purity to 98.25 percent purity, 98.25 percentpurity to 98.5 percent purity, 98.5 percent purity to 98.75 percentpurity, 98.75 percent purity to 99 percent purity, 99 percent purity to99.25 percent purity, 99.25 percent purity to 99.5 percent purity, 99.5percent purity to 99.75 percent purity, and 99.75 percent purity to 100percent purity.

In embodiments, a continuous process for the purification of cannabidioland/or tetrahydrocannabinol from a crude cannabinoid extract to providea purified cannabidiol and/or tetrahydrocannabinol product. The crudecannabinoid extract comprises cannabinoids which may include cannabidioland/or tetrahydrocannabinol.

In embodiments, reversed-phase chromatography employs a polar (aqueous)mobile phase. As a result, hydrophobic molecules in the polar mobilephase tend to adsorb to the hydrophobic stationary phase, andhydrophilic molecules in the mobile phase will pass through an adsorbercolumn and are eluted first.

The SMB system may be operated such that the adsorbent beds are operatedindividually or in parallel using a single rotary valve and associatedcontrol system. A column may comprise one or several beds containingchromatographic media. Feed tanks, filters, piping connecting flowbetween columns and/or beds where so connected, pumps, valving, pressureregulators, metering equipment, flow control and microprocessorequipment, their construction and function, and integration with theentire Farming Superstructure System (FSS) are all disclosed here.

Stationary Phase

In embodiments, the stationary phase adsorbent for use in the firstswing bed simulated moving bed (SMB) chromatography zone is an aromaticnon-polar copolymer of styrene-divinyl benzene adsorbent resin with aneffective particle size of 0.25 mm and effective surface area of 590square meters per gram (M2/g). Examples of suitable styrene-divinylbenzene adsorbent resins can be selected from the AMBERLITE XAD resinseries (Available from Dow Chemical Company, Midland, Mich.), DIAIONHP-20 (Available from Mitsubishi Chemical Company, Tokyo, Japan), orStratosphere PL-PS/DVB (Available from Sigma-Aldrich, St. Louis, Mo.).In embodiments, the styrene-divinyl benzene adsorbent resin matrixprovides an aromatic non-polar surface with selectivity for hydrophobicareas of molecules. In first swing bed simulated moving bed zone thecannabinoids are retained on the resin and are subsequently recovered ina first swing bed extract. Impurities such as wax, terpenes, and otherundesirable cannabinoids are rejected into a first swing bed raffinatestream. In first swing bed simulated moving bed zone the cannabinoidsare retained on the resin and are subsequently recovered in a firstswing bed extract. In first swing bed simulated moving bed zonecannabidiol is retained on the resin and are subsequently recovered in afirst swing bed extract. Impurities other cannabinoids are rejected intoa first swing bed raffinate stream. In first swing bed simulated movingbed zone tetrahydrocannabinol is retained on the resin and aresubsequently recovered in a first swing bed extract. Impurities othercannabinoids are rejected into a first swing bed raffinate stream. Thestationary phase adsorbents may be disposed in a single adsorbent bed ormay be disposed in within a single column or series of single columnscontaining multiple adsorbent bed zones.

In embodiments, the stationary phase adsorbent is comprised of one ormore selected from the group consisting of silica gel, alumina, silica,cellulose powder, a polymer, polymeric beads, a macroporous adsorptionresin, DOW XAD 418, molecular sieves, a polar macroporous adsorptionresin, floridin, diatomite, zeolites, a catalyst, a resin, anion-exchange resin, ion-exchange polymer, clay, ceramic material,activated carbon, a cation-exchange resin, an anion-exchange resin,bentonite, perlite, fly ash, chitin, charcoal, a solid substance,magnesia, titanium oxide, glass, fluorinated carbon, silicate, kaolin, ahollow substance, a porous substance.

In embodiments, the adsorbent includes Orpheus non-polar silica-basedstationary phase adsorbent (available from Orochem Technologies Inc.,Naperville, Ill., USA). In embodiments, the adsorbent includes C8, C18,or Polar C18 adsorbent (available from Orochem Technologies Inc.,Naperville, Ill., USA).

In embodiments, the adsorber or the plurality of adsorbers are comprisedof one or more corrosion resistant materials selected from the groupconsisting of stainless steel, corrosion resistant alloys, metals havinga fluoropolymer coating, and mixtures thereof. In embodiments, the valveused to connect each of the adsorbers is a rotary valve. In embodiments,the adsorber or the plurality of adsorbers are non-rotating and aredisposed in an asymmetrical manner about the axis of rotation of therotary valve. In embodiments, the rotary valve is actuated by eitherhydraulics, electricity, or electromechanical actuation.

In embodiments, the adsorbent is comprised of one or more selected fromthe group consisting of a strongly acidic ion-exchange resin, a stronglybasic ion-exchange resin, a weakly acidic ion-exchange resin and aweakly basic ion-exchange resin. In embodiments, the strongly acidicion-exchange resin includes sulfonic acid groups, e.g. sodiumpolystyrene sulfonate or PolyAMPS, orpoly(2-acrylamido-2-methyl-1-propanesulfonic acid)® (Trademark of TheLubrizol Corporation), is an organic polymer.

In embodiments, the strongly basic ion-exchange resin includesquaternary amino groups, for example, trimethylammonium groups, e.g.PolyAPTAC, or poly (acrylamido-N-propyltrimethylammonium chloride)®(Trademark of The Lubrizol Corporation), is an organic polymer. Inembodiments, the weakly acidic ion-exchange resin includes carboxylicacid groups. In embodiments, the weakly basic ion-exchange resinincludes primary, secondary, and/or tertiary amino groups, e.g.polyethylene amine.

In embodiments, the adsorbent is comprised of one or more selected fromthe group consisting of a powder, spheres, spherical pellets, rods,moldings, and monoliths. In embodiments, the adsorbent has pores. Inembodiments, the range of size of the pores of the adsorbent arecomprised of one or more selected from the group consisting of: 0.1nanometers to 1 nanometer, 1 nanometer to 2 nanometers, 2 nanometers to5 nanometers, 5 nanometers to 15 nanometers, 15 nanometers to 25nanometers, 25 nanometers to 35 nanometers, 35 nanometers to 40nanometers, 45 nanometers to 50 nanometers, 50 nanometers to 100nanometers, 100 nanometers to 150 nanometers, 150 nanometers to 200nanometers, 200 nanometers to 1000 nanometers, and greater than 1000nanometers.

In embodiments, the plurality of adsorbers are considered a simulatedmoving bed (SMB). In embodiments, the plurality of adsorbers areconsidered a simulated moving bed (SMB) and operate via chromatography.In embodiments, the SMB adsorption technique is a continuous. Inembodiments, the plurality of adsorbers include more than one adsorber.In embodiments, the plurality of adsorbers include two adsorbers. Inembodiments, the plurality of adsorbers include three adsorbers. Inembodiments, the plurality of adsorbers include four adsorbers. Inembodiments, the plurality of adsorbers include five adsorbers. Inembodiments, the plurality of adsorbers include six adsorbers. Inembodiments, the plurality of adsorbers include seven adsorbers. Inembodiments, the plurality of adsorbers include eight adsorbers. Inembodiments, the plurality of adsorbers include nine adsorbers. Inembodiments, the plurality of adsorbers include ten adsorbers. Inembodiments, the plurality of adsorbers include eleven adsorbers. Inembodiments, the plurality of adsorbers include twelve adsorbers. Inembodiments, the plurality of adsorbers include thirteen adsorbers. Inembodiments, the plurality of adsorbers include fourteen adsorbers. Inembodiments, the plurality of adsorbers include fifteen adsorbers. Inembodiments, the plurality of adsorbers include sixteen adsorbers. Inembodiments, the plurality of adsorbers include seventeen adsorbers. Inembodiments, the plurality of adsorbers include eighteen adsorbers. Inembodiments, the plurality of adsorbers include nineteen adsorbers. Inembodiments, the plurality of adsorbers include twenty adsorbers. Inembodiments, the plurality of adsorbers include twenty one adsorbers. Inembodiments, the plurality of adsorbers include twenty two adsorbers. Inembodiments, the plurality of adsorbers include twenty three adsorbers.In embodiments, the plurality of adsorbers include twenty fouradsorbers. In embodiments, the plurality of adsorbers include twentyfive adsorbers. In embodiments, the plurality of adsorbers includetwenty six adsorbers. In embodiments, the plurality of adsorbers includetwenty seven adsorbers. In embodiments, the plurality of adsorbersinclude twenty eight adsorbers. In embodiments, the plurality ofadsorbers include twenty nine adsorbers. In embodiments, the pluralityof adsorbers include thirty adsorbers. In embodiments, the plurality ofadsorbers include thirty one adsorbers. In embodiments, the plurality ofadsorbers include thirty two adsorbers. In embodiments, the plurality ofadsorbers include thirty three adsorbers. In embodiments, the pluralityof adsorbers include thirty four adsorbers. In embodiments, theplurality of adsorbers include thirty five adsorbers. In embodiments,the plurality of adsorbers include thirty six adsorbers. In embodiments,the plurality of adsorbers include thirty seven adsorbers. Inembodiments, the plurality of adsorbers include thirty eight adsorbers.In embodiments, the plurality of adsorbers include thirty nineadsorbers. In embodiments, the plurality of adsorbers include fortyadsorbers. In embodiments, the plurality of adsorbers include fiftyadsorbers. In embodiments, the plurality of adsorbers include sixtyadsorbers. In embodiments, the plurality of adsorbers include seventyadsorbers. In embodiments, the plurality of adsorbers include eightyadsorbers. In embodiments, the plurality of adsorbers include ninetyadsorbers. In embodiments, the plurality of adsorbers include onehundred adsorbers.

In embodiments, the adsorbers operate at a pressure that is selectedfrom one or more from the group consisting of between: 10 pounds persquare inch (PSI) to 20 PSI, 20 PSI to 40 PSI, 40 PSI to 60 PSI, 60 PSIto 80 PSI, 80 PSI to 100 PSI, 100 PSI to 125 PSI, 125 PSI to 150 PSI,150 PSI to 175 PSI, 175 PSI to 200 PSI, 200 PSI to 225 PSI, 225 PSI to250 PSI, 250 PSI to 275 PSI, 275 PSI to 300 PSI, 300 PSI to 325 PSI, 325PSI to 350 PSI, 350 PSI to 375 PSI, 375 PSI to 400 PSI, 400 PSI to 425PSI, 425 PSI to 450 PSI, 450 PSI to 475 PSI, and 475 PSI to 500 PSI.

In embodiments, an analyzer is used to analyze the purified cannabidioland/or tetrahydrocannabinol product. In embodiments, the analyzer iscomprised of one or more analyzers selected from the group consisting ofFourier-transform infrared spectroscopy, gas chromatography,high-performance liquid chromatography, liquid chromatograph, liquidchromatography-mass spectrometry, mass spectrometry, and ultra-highperformance liquid chromatography.

In embodiments, the adsorbent is comprised of one or more selected fromthe group consisting of a strongly acidic cation exchange resin includesuch as AMBERLITE IR-118 (Available from Dow Chemical Company, Midland,Mich.), or DIAION PK216LH (Available from Mitsubishi Chemical Company,Tokyo, Japan). Suitable examples of the weakly basic anion exchangeresin include AMBERLITE IRA-70RF (Available from Dow Chemical Company,Midland, Mich.) or RELITE RAM2 (Available from Mitsubishi ChemicalCompany, Tokyo, Japan).

In embodiments, the first extract (HDA) or the primary extract (HDB) istransferred from the first adsorber system (SMB1) and into a primaryextract vessel (HEE). In embodiments, the first raffinate (HDE) istransferred from the first adsorber system (SMB1) into the solventtreatment system (H-WTS) as discussed below.

In embodiments, the primary extract vessel (HEE) has an interior (HEF).In embodiments, the primary extract vessel (HEE) is a continuouslystirred tank reactor having a jacketed reactor equipped with a steamsupply system and at least one steam trap. In embodiments, the primaryextract vessel (HEE) is equipped with a level sensor (HEG) that isconfigured to input a signal to the computer (COMP). In embodiments, theprimary extract vessel (HEE) is equipped with a pH sensor (HEH) that isconfigured to input a signal to the computer (COMP). In embodiments, theprimary extract vessel (HEE) is equipped with an auger (HEI) that has amotor. The motor of the auger (HEI) rotates the auger (HEI) to mix thecontents within the interior (HEF) of the primary extract vessel (HEE).In embodiments, the primary extract vessel (HEE) is equipped with atemperature sensor that is configured to input a signal to the computer(COMP). In embodiments, the primary extract vessel (HEE) is equippedwith a heat exchanger (HTA) to heat and/or cool the contents within theinterior (HEF) of the primary extract vessel (HEE). In embodiments, theprimary extract vessel (HEE) outputs a primary extract (HDB).

A primary extract pump (HTB) is configured to accept the primary extract(HDB) from the interior (HEF) of the primary extract vessel (HEE). Theprimary extract pump (HTB) pumps and pressurizes the primary extract(HDB) to produce a pressurized primary extract (HTC). A valve (HTD) anda pressure sensor (HTE) are installed on the discharged of the primaryextract pump (HTB). In embodiments, the primary extract pump (HTB)pressurizes the primary extract (HDB) to form a pressurized primaryextract (HTC) at a pressure that includes one or more pressure rangesselected from the group consisting of 10 pounds per square inch (PSI) to20 PSI, 20 PSI to 40 PSI, 40 PSI to 60 PSI, 60 PSI to 80 PSI, 80 PSI to100 PSI, 100 PSI to 125 PSI, 125 PSI to 150 PSI, 150 PSI to 175 PSI, 175PSI to 200 PSI, 200 PSI to 225 PSI, 225 PSI to 250 PSI, 250 PSI to 275PSI, 275 PSI to 300 PSI, 300 PSI to 325 PSI, 325 PSI to 350 PSI, 350 PSIto 375 PSI, 375 PSI to 400 PSI, 400 PSI to 425 PSI, 425 PSI to 450 PSI,450 PSI to 475 PSI, and 475 PSI to 500 PSI.

In embodiments, the pressurized primary extract (HTC) is transferredfrom the primary extract pump (HTB) and into at least one filter (HEL,HEM, HEN). In embodiments, the pressurized primary extract (HTC) istransferred from the primary extract pump (HTB) and a primary extractfilter system (HEK) that includes a first primary extract first filter(HEL), a first primary extract second filter (HEM), and a first primaryextract third filter (HEN).

In embodiments, the first primary extract first filter (HEL) includesone or more selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the first primary extract second filter (HEM)includes one or more selected from the group consisting of a cation, ananion, a membrane, a filter, activated carbon, an adsorbent, anabsorbent, an ultraviolet unit, an ozone unit, a microwave unit, and/ora distillation system. In embodiments, the first primary extract thirdfilter (HEN) includes one or more selected from the group consisting ofa cation, an anion, a membrane, a filter, activated carbon, anadsorbent, an absorbent, an ultraviolet unit, an ozone unit, a microwaveunit, and/or a distillation system. In embodiments, the adsorbentincludes one or more selected from the group consisting of 3 Angstrommolecular sieve, 3 Angstrom zeolite, 4 Angstrom molecular sieve, 4Angstrom zeolite, activated alumina, activated carbon, adsorbent,alumina, carbon, catalyst, clay, desiccant, molecular sieve, polymer,resin, and silica gel.

In embodiments, the cation is configured to remove positively chargedions from the pressurized primary extract (HTC), the positively chargedions are comprised of one or more from the group consisting of calcium,magnesium, sodium, and iron. In embodiments, the anion is configured toremove negatively charged ions from the pressurized primary extract(HTC), the negatively charged ions are comprised of one or more from thegroup consisting of iodine, chloride, and sulfate. In embodiments, themembrane is configured to remove undesirable compounds from thepressurized primary extract (HTC), the undesirable compounds arecomprised of one or more from the group consisting of dissolved organicchemicals, viruses, bacteria, and particulates. In embodiments, themembrane has a diameter that ranges from 1 inch to 6 inches and a poresize ranging from 0.0001 microns to 0.5 microns.

In embodiments, a filtered primary extract (HEO) is discharged from theprimary extract filter system (HEK). In embodiments, the filteredprimary extract (HEO) discharged from the primary extract filter system(HEK) is a pressurized filtered primary extract (HEP). In embodiments, avalve (HEQ) is configured to regulate the flow of the pressurizedfiltered primary extract (HEP) that leaves the primary extract filtersystem (HEK). In embodiments, a pressure sensor (HER) is configured tomeasure the pressure of the pressurized filtered primary extract (HEP).

In embodiments, the pressurized filtered primary extract (HEP) is passedfrom the primary extract filter system (HEK) and into a filtered primaryextract vessel (HES). In embodiments, filtered primary extract vessel(HES) is configured to accept the filtered primary extract (HEO). Inembodiments, the filtered primary extract vessel (HES) is a continuouslystirred tank reactor having a jacketed reactor equipped with a steamsupply system and at least one steam trap. In embodiments, the filteredprimary extract vessel (HES) is equipped with a level sensor (HEU) thatis configured to input a signal to the computer (COMP). In embodiments,the filtered primary extract vessel (HES) is equipped with a pH sensor(HEV) that is configured to input a signal to the computer (COMP). Inembodiments, the filtered primary extract vessel (HES) is equipped withan auger (HEW) that has a motor. The motor of the auger (HEW) rotatesthe auger (HEW) to mix the contents within the interior (HET) of thefiltered primary extract vessel (HES). In embodiments, the filteredprimary extract vessel (HES) is equipped with a temperature sensor thatis configured to input a signal to the computer (COMP). In embodiments,the filtered primary extract vessel (HES) is equipped with a heatexchanger (HEX) to heat and/or cool the contents within the interior(HET) of the filtered primary extract vessel (HES). In embodiments, thefiltered primary extract vessel (HES) outputs a filtered primaryextract.

In embodiments, a filtered primary extract is discharged from theinterior (HET) of the filtered primary extract vessel (HES). Inembodiments, a filtered primary extract is discharged from the interior(HET) of the filtered primary extract vessel (HES) and introduced to afiltered primary extract pump (HEY). The filtered primary extract pump(HEY) pumps and pressurizes the filtered primary extract to form apressurized filtered primary extract (HEZ). In embodiments, a valve(HFA) is configured to regulate the flow of the pressurized filteredprimary extract (HEZ) that leaves the filtered primary extract vessel(HES). In embodiments, a pressure sensor (HFB) is configured to measurethe pressure of the pressurized filtered primary extract (HEZ)discharged from the filtered primary extract pump (HEY). In embodiments,a flow sensor (HFC) is configured to measure the flow of the pressurizedfiltered primary extract (HEZ) discharged from the filtered primaryextract pump (HEY).

In embodiments, the pressurized filtered primary extract (HEZ) istransferred from the filtered primary extract pump (HEY) and into asecond adsorber system (SMB2). In embodiments, the second adsorbersystem (SMB2) is configured to input a pressurized filtered primaryextract (HEZ) and a second desorbent (HFG). In embodiments, the secondadsorber system (SMB2) is configured to output a second extract (HFD)and a second raffinate (HFH). In embodiments, the second extract (HFD)can also be called a secondary extract (HFE). In embodiments, the secondadsorber system (SMB2) includes an adsorber or a plurality of adsorberseach containing an adsorbent. In embodiments, the second desorbent (HFG)is pressurized and comes from a water treatment system (H-WTS) which mayor may not treat solvent (such as water) that was passed on from asolvent recovery system. In embodiments, the second raffinate (HFH) isrouted to the solvent treatment system (H-WTS) as discussed below.

In embodiments, the second adsorber system (SMB2) includes a pluralityof adsorbers containing adsorbent is provided and may be called thestationary phase. In embodiments, the adsorbent positioned within theadsorber or plurality of adsorbers may be called the stationary phase.The bed of adsorbent that is contained within the adsorber does not moveso therefore it is stationary. The plurality of beds of adsorbent thatare contained within the plurality of adsorbers does not move sotherefore it is stationary.

In embodiments, the second adsorber system (SMB2) periodically switchesthe feed, eluent, extract and raffinate ports in the same direction. Thebasic premise of a simulated moving bed adsorber system is that theinlet and outlet ports are switched periodically in the direction of thefluid flow. This simulates the countercurrent movement of the phase inthe process. Chromatography is a technique used to separate mixtures. Inembodiments, the mixture may include cannabinoids and a solvent.

In embodiments, the raffinate includes cannabinoids. In embodiments, theraffinate includes cannabidiol. In embodiments, the raffinate includesTHC. In embodiments, the raffinate includes a mixture of cannabinoidsand water. In embodiments, the raffinate includes a mixture ofcannabidiol and water. In embodiments, the raffinate includes a mixtureof THC and water. In embodiments, the raffinate includes a mixture ofcannabinoids and ethanol. In embodiments, the raffinate includes amixture of cannabidiol and ethanol. In embodiments, the raffinateincludes a mixture of THC and ethanol. In embodiments, the raffinateincludes a mixture of cannabinoids and ethanol and water. Inembodiments, the raffinate includes a mixture of cannabidiol and ethanoland water. In embodiments, the raffinate includes a mixture of THC andethanol and water. In embodiments, the raffinate includes a mixture ofcannabinoids and methanol. In embodiments, the raffinate includes amixture of cannabidiol and methanol. In embodiments, the raffinateincludes a mixture of THC and methanol.

In embodiments, the raffinate includes a mixture of cannabinoids andmethanol and water. In embodiments, the raffinate includes a mixture ofcannabidiol and methanol and water. In embodiments, the raffinateincludes a mixture of THC and methanol and water.

In embodiments, the second extract (HFD) or the secondary extract (HFE)is transferred from the second adsorber system (SMB2) and into asecondary extract vessel (HFI). In embodiments, the second raffinate(HFH) is transferred from the second adsorber system (SMB2) into thesolvent treatment system (H-WTS) as discussed below.

In embodiments, the secondary extract vessel (HFI) has an interior(HFJ). In embodiments, the secondary extract vessel (HFI) is acontinuously stirred tank reactor having a jacketed reactor equippedwith a steam supply system and at least one steam trap. In embodiments,the secondary extract vessel (HFI) is equipped with a level sensor (HFK)that is configured to input a signal to the computer (COMP). Inembodiments, the secondary extract vessel (HFI) is equipped with a pHsensor (HFL) that is configured to input a signal to the computer(COMP). In embodiments, the secondary extract vessel (HFI) is equippedwith an auger that has a motor. The motor of the auger rotates the augerto mix the contents within the interior (HFJ) of the secondary extractvessel (HFI). In embodiments, the secondary extract vessel (HFI) isequipped with a temperature sensor that is configured to input a signalto the computer (COMP). In embodiments, the secondary extract vessel(HFI) is equipped with a heat exchanger (HFN) to heat and/or cool thecontents within the interior (HFJ) of the secondary extract vessel(HFI). In embodiments, the secondary extract vessel (HFI) outputs asecondary extract.

A secondary extract pump (HFO) is configured to accept the secondextract from the interior (HFJ) of the secondary extract vessel (HFI).The secondary extract pump (HFO) pumps and pressurizes the secondaryextract to produce a pressurized secondary extract (HFP). A valve (HFQ)and a pressure sensor (HFR) are installed on the discharged of thesecondary extract pump (HFO). In embodiments, the secondary extract pump(HFO) pressurizes the secondary extract to form a pressurized secondaryextract (HFP) at a pressure that includes one or more pressure rangesselected from the group consisting of 10 pounds per square inch (PSI) to20 PSI, 20 PSI to 40 PSI, 40 PSI to 60 PSI, 60 PSI to 80 PSI, 80 PSI to100 PSI, 100 PSI to 125 PSI, 125 PSI to 150 PSI, 150 PSI to 175 PSI, 175PSI to 200 PSI, 200 PSI to 225 PSI, 225 PSI to 250 PSI, 250 PSI to 275PSI, 275 PSI to 300 PSI, 300 PSI to 325 PSI, 325 PSI to 350 PSI, 350 PSIto 375 PSI, 375 PSI to 400 PSI, 400 PSI to 425 PSI, 425 PSI to 450 PSI,450 PSI to 475 PSI, and 475 PSI to 500 PSI.

In embodiments, the pressurized secondary extract (HFP) is transferredfrom the secondary extract pump (HFO) and into a secondary extractfilter system (HGA). In embodiments, the secondary extract filter system(HGA) includes one or more selected from the group consisting of acation, an anion, a membrane, a filter, activated carbon, an adsorbent,an absorbent, an ultraviolet unit, an ozone unit, a microwave unit,and/or a distillation system. In embodiments, the adsorbent includes oneor more selected from the group consisting of 3 Angstrom molecularsieve, 3 Angstrom zeolite, 4 Angstrom molecular sieve, 4 Angstromzeolite, activated alumina, activated carbon, adsorbent, alumina,carbon, catalyst, clay, desiccant, molecular sieve, polymer, resin, andsilica gel.

In embodiments, a filtered secondary extract (HGB) is discharged fromthe secondary extract filter system (HGA). In embodiments, the filteredsecondary extract (HGB) is transferred to a filtered secondary extractvessel (HGD). In embodiments, the filtered secondary extract vessel(HGD) has an interior (HGE). In embodiments, the filtered secondaryextract vessel (HGD) is a continuously stirred tank reactor having ajacketed reactor equipped with a steam supply system and at least onesteam trap. In embodiments, the filtered secondary extract vessel (HGD)is equipped with a level sensor (HGF) that is configured to input asignal to the computer (COMP). In embodiments, the filtered secondaryextract vessel (HGD) is equipped with a pH sensor that is configured toinput a signal to the computer (COMP). In embodiments, the filteredsecondary extract vessel (HGD) is equipped with an auger that has amotor. The motor of the auger rotates the auger to mix the contentswithin the interior (HGE) of the filtered secondary extract vessel(HGD). In embodiments, the filtered secondary extract vessel (HGD) isequipped with a temperature sensor that is configured to input a signalto the computer (COMP). In embodiments, the filtered secondary extractvessel (HGD) is equipped with a heat exchanger (HGG) to heat and/or coolthe contents within the interior (HGE) of the filtered secondary extractvessel (HGD). In embodiments, the filtered secondary extract vessel(HGD) outputs a first pressurized filtered secondary extract (HGJ) and asecond pressurized filtered secondary extract (HGK). In embodiments, theheat exchangers (HAM, HCL, HTA, HEX, HGA, HGG) shown in FIG. 17H′ mayheat and/or cool the cannabis, cannabinoid, crude oil and solventmixture.

In embodiments, the heat exchangers (HAM, HCL, HTA, HEX, HGA, HGG) maydecarboxylates the cannabis to produce a decarboxylated cannabis. Inembodiments, heating the cannabis, cannabinoid, crude oil and solventmixture decarboxylates the tetrahydrocannabinolic acid to form activetetrahydrocannabinol. In embodiments, decarboxylation is a chemicalreaction that removes a carboxyl group and releases carbon dioxide. Inembodiments, heating the cannabis removes carbon dioxide form thecannabis to form a carbon dioxide depleted cannabis.

In embodiments, the first pressurized filtered secondary extract (HGJ)is discharged from the interior (HGE) of the filtered secondary extractvessel (HGD) and transferred to a first filtered secondary extract pump(HGH). The first filtered secondary extract pump (HGH) pumps andpressurizes the filtered secondary extract to produce a firstpressurized filtered secondary extract (HGJ).

In embodiments, the first pressurized filtered secondary extract (HGJ)may be transferred to FIGS. 17D′, 17E′, 17J′, and/or FIG. 18′ or anyfigure in this patent specification for evaporation, spray drying,emulsion mixing, encapsulation, and foodstuff mixing. In embodiments,the second pressurized filtered secondary extract (HGK) is dischargedfrom the interior (HGE) of the filtered secondary extract vessel (HGD)and transferred to a second filtered secondary extract pump (HGI). Thesecond filtered secondary extract pump (HGI) pumps and pressurizes thefiltered secondary extract to produce a second pressurized filteredsecondary extract (HGK). In embodiments, the second pressurized filteredsecondary extract (HGK) may be transferred to a third adsorber system(SMB3).

In embodiments, the secondary extract (HGL) is transferred from theinterior (HGE) of the filtered secondary extract vessel (HGD) and into asecond filtered secondary extract pump (HGI). The second filteredsecondary extract pump (HGI) pumps and pressurizes the filteredsecondary extract to produce a second pressurized filtered secondaryextract (HGK). In embodiments, a valve (HGM) is configured to regulatethe flow of the second pressurized filtered secondary extract (HGK) thatleaves the filtered secondary extract vessel (HGD). In embodiments, apressure sensor (HFB) is configured to measure the pressure of thesecond pressurized filtered secondary extract (HGK) discharged from thesecond filtered secondary extract pump (HGI). In embodiments, a flowsensor (HFC) is configured to measure the flow of the second pressurizedfiltered secondary extract (HGK) discharged from the second filteredsecondary extract pump (HGI).

In embodiments, the second pressurized filtered secondary extract (HGK)is transferred from the second filtered secondary extract pump (HGI) andinto a third adsorber system (SMB3). In embodiments, the third adsorbersystem (SMB3) is configured to input a second pressurized filteredsecondary extract (HGK) and a third desorbent (HHC). In embodiments, thethird adsorber system (SMB3) is configured to output a third extract(HHA) and a third raffinate (HHD). In embodiments, the third extract(HHA) can also be called a tertiary extract (HHB). In embodiments, thethird adsorber system (SMB3) includes an adsorber or a plurality ofadsorbers each containing an adsorbent. In embodiments, the thirddesorbent (HHC) is pressurized and comes from a water treatment system(H-WTS) which may or may not treat solvent (such as water) that waspassed on from a solvent recovery system. In embodiments, the thirdraffinate (HHD) is routed to the solvent treatment system (H-WTS) asdiscussed below.

In embodiments, the third adsorber system (SMB3) includes a plurality ofadsorbers containing adsorbent is provided and may be called thestationary phase. In embodiments, the adsorbent positioned within theadsorber or plurality of adsorbers may be called the stationary phase.The bed of adsorbent that is contained within the adsorber does not moveso therefore it is stationary. The plurality of beds of adsorbent thatare contained within the plurality of adsorbers does not move sotherefore it is stationary.

In embodiments, the third adsorber system (SMB3) periodically switchesthe feed, eluent, extract and raffinate ports in the same direction. Thebasic premise of a simulated moving bed adsorber system is that theinlet and outlet ports are switched periodically in the direction of thefluid flow. This simulates the countercurrent movement of the phase inthe process. Chromatography is a technique used to separate mixtures. Inembodiments, the mixture may include cannabinoids and a solvent. Inembodiments, the third extract (HHA) may be transferred to FIGS. 17D′,17E′, 17J′, and/or FIG. 18′ or any figure in this patent specificationfor evaporation, spray drying, emulsion mixing, encapsulation, andfoodstuff mixing.

In embodiments, the first desorbent (HDC) for the first adsorber system(SMB1), second desorbent (HFG) for the second adsorber system (SMB2),third desorbent (HHC) for the third adsorber system (SMB3), are providedby a solvent treatment system (H-WTS).

In embodiments, the solvent (HBJ) from the first filter (HBC) and/orsecond filter (HBF), the first raffinate (HDE) from the first adsorbersystem (SMB1), the second raffinate (HFH) from the second adsorbersystem (SMB2), and the third raffinate (HHD) from the third adsorbersystem (SMB3), are provided by to a solvent treatment system (H-WTS). Inembodiments, the solvent treatment system (H-WTS) includes a treatmentunit (HIC). In embodiments, the treatment unit (HIC) includes one ormore selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the adsorbent includes one or more selected fromthe group consisting of 3 Angstrom molecular sieve, 3 Angstrom zeolite,4 Angstrom molecular sieve, 4 Angstrom zeolite, activated alumina,activated carbon, adsorbent, alumina, carbon, catalyst, clay, desiccant,molecular sieve, polymer, resin, and silica gel. In embodiments, thetreatment unit (HIC) includes one or more selected from the groupconsisting of an evaporator, an anaerobic digestion system, adistillation column, a packed column, a reactor, liquid-liquidextraction, vacuum distillation, pressurized distillation, and reverseosmosis.

In embodiments, the first desorbent (HDC) for the first adsorber system(SMB1), second desorbent (HFG) for the second adsorber system (SMB2),third desorbent (HHC) for the third adsorber system (SMB3), are providedby a solvent treatment system (H-WTS). In embodiments, the solvent (HBJ)from the first filter (HBC) and/or second filter (HBF), the firstraffinate (HDE) from the first adsorber system (SMB1), the secondraffinate (HFH) from the second adsorber system (SMB2), and the thirdraffinate (HHD) from the third adsorber system (SMB3), are provided byto a solvent treatment system (H-WTS). In embodiments, a treated solvent(HIE) is discharged from the treatment unit (HIC) of the solventtreatment system (H-WTS). In embodiments, the treated solvent (HIE) hascontaminants removed therefrom so that the solvent (water, ethanol,alcohol, oil, etc.) may be reused again in the solvent (HAB, HAB′) orfor the first desorbent (HDC) for the first adsorber system (SMB1),second desorbent (HFG) for the second adsorber system (SMB2), thirddesorbent (HHC) for the third adsorber system (SMB3).

In embodiments, the solvent (HAB′) used within the extraction vessel(HAI) is water that comes from the solvent treatment system (H-WTS). Inembodiments, a water supply (HJG) is made available to the solventtreatment system (H-WTS) for use as either a solvent (HAB′HAB′) in theprocess or for use as the first desorbent (HDC) for the first adsorbersystem (SMB1), second desorbent (HFG) for the second adsorber system(SMB2), third desorbent (HHC) for the third adsorber system (SMB3). Inembodiments, the water supply (HJG) is mixed with the treated solvent(HIE) (which may be water). In embodiments, a valve (HJI) is configuredto regulate the flow of the water supply (HJG) that enters the firstwater treatment unit (HJK) of the solvent treatment system (H-WTS). Inembodiments, a pressure sensor (HJH) is configured to measure thepressure of the water supply (HJG) that enters the first water treatmentunit (HJK) of the solvent treatment system (H-WTS). In embodiments, thesolvent treatment system (H-WTS) includes a first water treatment unit(HJK), second water treatment unit (HJL), and a third water treatmentunit (HJM).

In embodiments, the first water treatment unit (HJK) includes one ormore selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the second water treatment unit (HJL) includesone or more selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the third water treatment unit (HJM) includesone or more selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the adsorbent includes one or more selected fromthe group consisting of 3 Angstrom molecular sieve, 3 Angstrom zeolite,4 Angstrom molecular sieve, 4 Angstrom zeolite, activated alumina,activated carbon, adsorbent, alumina, carbon, catalyst, clay, desiccant,molecular sieve, polymer, resin, and silica gel. In embodiments, thecation is configured to remove positively charged ions from the watersupply (HJG), the positively charged ions are comprised of one or morefrom the group consisting of calcium, magnesium, sodium, and iron. Inembodiments, the anion is configured to remove negatively charged ionsfrom the water supply (HJG), the negatively charged ions are comprisedof one or more from the group consisting of iodine, chloride, andsulfate. In embodiments, the membrane is configured to removeundesirable compounds from the water supply (HJG), the undesirablecompounds are comprised of one or more from the group consisting ofdissolved organic chemicals, viruses, bacteria, and particulates. Inembodiments, the membrane has a diameter that ranges from 1 inch to 6inches and a pore size ranging from 0.0001 microns to 0.5 microns.

In embodiments, treated water (HJA) is discharged from the first watertreatment unit (HJK), second water treatment unit (HJL), and/or thethird water treatment unit (HJM). In embodiments, treated water (HJA)has less positively charged ions, negatively charged ions, andundesirable compounds relative to the supply (HJG) that enters thesolvent treatment system (H-WTS). In embodiments, a valve (HJI) isconfigured to regulate the flow of the treated water (HJA) that leavesthe first water treatment unit (HJK), second water treatment unit (HJL),and/or the third water treatment unit (HJM). In embodiments, a qualitysensor (HJN) is configured to measure the quality of the treated water(HJA) that leaves the first water treatment unit (HJK), second watertreatment unit (HJL), and/or the third water treatment unit (HJM). Forexample, the quality sensor (HJN) may measure the electricalconductivity of the treated water (HJA) to determine if either of thefirst water treatment unit (HJK), second water treatment unit (HJL),and/or the third water treatment unit (HJM) require maintenance and/orcleaning. In embodiments, the quality sensor (HJN) measures theelectrical conductivity of the treatment unit (HJM) to ensure that theelectrical conductivity ranges from 0.10 microsiemens per centimeter to100 microsiemens per centimeter.

In embodiments, the quality sensor (HJN) measures the electricalconductivity of the treatment unit (HJM) to ensure that the electricalconductivity ranges from one or more selected from the group consistingof 0.1 μS to 0.5 μS, 0.5 μS to 1.00 μS, 1.00 μS to 1.25 μS, 1.25 μS to1.50 μS, 1.50 μS to 1.75 μS, 1.75 μS to 2.00 μS, 2.0 μS to 2.25 μS,2.250 to 2.50 μS, 2.50 μS to 2.75 μS, 2.75 μS to 3.00 μS, 3.00 μS to3.25 μS, 3.25 μS to 3.50 μS, 3.50 μS to 3.75 μS, 3.75 μS to 4.00 μS,4.00 μS to 4.25 μS, 4.25 μS to 4.50 μS, 4.50 μS to 4.75 μS, 4.75 μS to5.00 μS, 5.00 μS to 5.25 μS, 5.25 μS to 5.50 μS, 5.50 μS to 5.75 μS,5.75 μS to 6.00 μS, 6.00 μS to 6.25 μS, 6.25 μS to 6.50 μS, 6.50 μS to6.75 μS, 6.75 μS to 7.00 μS, 7.00 μS to 7.25 μS, 7.25 μS to 7.50 μS,7.50 μS to 7.75 μS, 7.75 μS to 8.00 μS, 8.00 μS to 8.25 μS, 8.25 μS to8.50 μS, 8.50 μS to 8.75 μS, 8.75 μS to 9.00 μS, 9.00 μS to 9.25 μS,9.25 μS to 9.50 μS, 9.50 μS to 9.75 μS, 9.75 μS to 10.00 μS, 10.00 μS to12.50 μS, 12.50 μS to 15.00 μS, 15.00 μS to 17.50 μS, 17.50 μS to 20.00μS, 20.00 μS to 22.50 μS, 22.50 μS to 25.00 μS, 25.00 μS to 27.50 μS,27.50 μS to 30.00 μS, 30.00 μS to 32.50 μS, 32.50 μS to 35.00 μS, 35.00μS to 37.50 μS, 37.50 μS to 40.00 μS, 40.00 μS to 42.50 μS, 42.50 μS to45.00 μS, 45.00 μS to 47.50 μS, 47.50 μS to 50.00 μS, 50.00 μS to 52.50μS, 52.50 μS to 55.00 μS, 55.00 μS to 57.50 μS, 57.50 μS to 60.00 μS,60.00 μS to 62.50 μS, 62.50 μS to 65.00 μS, 65.00 μS to 67.50 μS, 67.50μS to 70.00 μS, 70.00 μS to 72.50 μS, 72.50 μS to 75.00 μS, 75.00 μS to77.50 μS, and 77.50 μS to 100.00 μS. In embodiments, μS means μS percentimeter.

In embodiments, the treated water used in the nanoemulsion process,cannabis cloning/irrigation, insect water source, etc. may in someinstances conform to the following specifications: Bicarbonate (25 to500 mg/L), Calcium (5 to 100 mg/L), Chloride (1 to 25 mg/L), Magnesium(1 to 25 mg/L), Sodium (1 to 25 mg/L), Sulfate (0.05 to 3 mg/L), TotalDissolved Solids (15 to 500 mg/L), Total Alkalinity (25 to 300 mg/L).

In embodiments, the treated solvent (HIE) is transferred from the firstwater treatment unit (HJK), second water treatment unit (HJL), or thirdwater treatment unit (HJM) and into a treated water vessel (HJF). Inembodiments, the treated water vessel (HJF) has an interior. Inembodiments, the treated water vessel (HJF) is a continuously stirredtank reactor having a jacketed reactor equipped with a steam supplysystem and at least one steam trap. In embodiments, the treated watervessel (HJF) is equipped with a level sensor (HJPP) that is configuredto input a signal to the computer (COMP). In embodiments, the treatedwater vessel (HJF) is equipped with a pH sensor (HJQ) that is configuredto input a signal to the computer (COMP). In embodiments, the treatedwater vessel (HJF) is equipped with an auger that has a motor. The motorof the auger rotates the auger to mix the contents within the interiorof the treated water vessel (HJF). In embodiments, the treated watervessel (HJF) is equipped with a temperature sensor that is configured toinput a signal to the computer (COMP). In embodiments, the treated watervessel (HJF) is equipped with a heat exchanger to heat the contentswithin the interior of the treated water vessel (HJF). In embodiments,the treated water vessel (HJF) outputs treated water (HJA).

In embodiments, the treated water (HJA) discharged from the treatedwater vessel (HJF) is provided to a treated water pump (HJD). Inembodiments, the treated water pump (HJD) pumps and pressurizes thetreated water (HJA) to form pressurized treated water (HJB). Inembodiments, the pressurized treated water (HJB) provided by the treatedwater pump (HJD) is made available to the interior (HAJ) extraction zone(HAI′) as a solvent (HAB′). In embodiments, the pressurized treatedwater (HJB) provided by the treated water pump (HJD) is made availablefor use as the first desorbent (HDC) for the first adsorber system(SMB1), second desorbent (HFG) for the second adsorber system (SMB2),third desorbent (HHC) for the third adsorber system (SMB3). Inembodiments, a treated water valve (HJE) is configured to regulate theflow of the pressurized treated water (HJB) that leaves the solventtreatment system (H-WTS). In embodiments, a pressure sensor (HJH) isconfigured to measure the pressure of the pressurized treated water(HJB) that is discharged from the treated water pump (HJD). Inembodiments, a pH adjustment solution (HJR) is made available to thetreated water vessel (HJF). In embodiments, the pH adjustment solution(HJR) passes through a valve (HJS) prior to being introduced to theinterior of the treated water vessel (HJF).

In embodiments, the treated water (HJA) within the treated water vessel(HJF) is preferably maintained at a pH of 6.1 to 6.8. In embodiments,the treated water (HJA) within the treated water vessel (HJF) ispreferably maintained at a pH including one or more selected from thegroup consisting of 5.00 to 5.05, 5.05 to 5.10, 5.10 to 5.15, 5.15 to5.20, 5.20 to 5.25, 5.25 to 5.30, 5.30 to 5.35, 5.35 to 5.40, 5.40 to5.45, 5.45 to 5.50, 5.50 to 5.55, 5.55 to 5.60, 5.60 to 5.65, 5.65 to5.70, 5.70 to 5.75, 5.75 to 5.80, 5.80 to 5.85, 5.85 to 5.90, 5.90 to5.95, 5.95 to 6.00, 6.00 to 6.05, 6.05 to 6.10, 6.10 to 6.15, 6.15 to6.20, 6.20 to 6.25, 6.25 to 6.30, 6.30 to 6.35, 6.35 to 6.40, 6.40 to6.45, 6.45 to 6.50, 6.50 to 6.55, 6.55 to 6.60, 6.60 to 6.65, 6.65 to6.70, 6.70 to 6.75, 6.75 to 6.80, 6.80 to 6.85, 6.85 to 6.90, and 6.90to 6.95.

In embodiments, the pH adjustment solution (HJR) is comprised of one ormore from the group consisting of acid, nitric acid, phosphoric acid,potassium hydroxide, sulfuric acid, organic acids, citric acid, andacetic acid.

FIG. 17J′

FIG. 17J′ shows one non-limiting embodiment of a cannabinoid emulsionmixing system.

Cannabinoids (THC, CBD, etc.) are lipophilic and hydrophobic.Cannabinoids such as THC and CDB are lipophilic and that they tend tocombine with or dissolve in each other or in other compounds such aslipids or fats. Cannabinoids such as THC and CDB are hydrophobic andthey tend to repel or fail to mix with water. An emulsion is a mixtureof water and cannabinoids. An emulsion can be prepared from treatedwater having an electrical conductivity ranging from 0.10 microsiemensper centimeter to 100 microsiemens per centimeter.

In embodiments, the emulsion mixing system shown in FIG. 17J′ isspecially equipped with a purge system to provide inert gases to theinterior of the system to form a protective atmosphere (preventoxidation and/or degradation of the emulsion or ingredients, improvedproduct quality, clean good manufacturing practices as required bypharmaceutical industry, for cleaning in place, etc.) while creating theemulsion.

In embodiments, the emulsion mixing system shown in FIG. 17J′ creates ananoemulsion is thermodynamically stable. In embodiments, the emulsionproduced has the following characteristics:

(i) a pH ranging from one or more selected from the group consisting of6 to 6.25, 6.25 to 6.5, 6.5 to 6.75, 6.75 to 7, 7 to 7.05, 7.05 to 7.1,7.1 to 7.15, 7.15 to 7.2, 7.2 to 7.25, 7.25 to 7.3, 7.3 to 7.35, 7.35 to7.4, 7.4 to 7.45, 7.45 to 7.5, 7.5 to 7.55, 7.55 to 7.6, 7.6 to 7.65,7.65 to 7.7, 7.7 to 7.75, 7.75 to 7.8, 7.8 to 7.85, 7.85 to 7.9, 7.9 to7.95, 7.95 to 8, 8 to 8.05, 8.05 to 8.1, 8.1 to 8.15, 8.15 to 8.2, 8.2to 8.25, 8.25 to 8.3, 8.3 to 8.35, 8.35 to 8.4, 8.4 to 8.45, 8.45 to8.5, and 8.5 to 9.

(ii) a viscosity ranging from one or more selected from the groupconsisting of 0.9 centipoise (cps) to 1 cps, 1 cps to 1.1 cps, 1.1 cpsto 1.2 cps, 1.2 cps to 1.3 cps, 1.3 cps to 1.4 cps, 1.4 cps to 1.5 cps,1.5 cps to 1.6 cps, 1.6 cps to 1.7 cps, 1.7 cps to 1.8 cps, 1.8 cps to1.9 cps, 1.9 cps to 2 cps, 2 cps to 2.1 cps, 2.1 cps to 2.2 cps, 2.2 cpsto 2.3 cps, 2.3 cps to 2.4 cps, 2.4 cps to 2.5 cps, 2.5 cps to 2.6 cps,2.6 cps to 2.7 cps, 2.7 cps to 2.8 cps, 2.8 cps to 2.9 cps, 2.9 cps to 3cps, 3 cps to 5 cps, 5 cps to 10 cps, 10 cps to 20 cps, 20 cps to 30cps, 30 cps to 40 cps, 40 cps to 50 cps, 50 cps to 60 cps, 60 cps to 70cps, 70 cps to 80 cps, 80 cps to 90 cps, 90 cps to 100 cps, 100 cps to125 cps, 125 cps to 150 cps, 150 cps to 175 cps, 175 cps to 200 cps, 200cps to 225 cps, 225 cps to 250 cps, 250 cps to 275 cps, 275 cps to 300cps, 300 cps to 325 cps, 325 cps to 350 cps, 350 cps to 375 cps, 375 cpsto 400 cps, 400 cps to 425 cps, 425 cps to 450 cps, 450 cps to 475 cps,475 cps to 500 cps, 500 cps to 550 cps, 550 cps to 600 cps, 600 cps to650 cps, 650 cps to 700 cps, 700 cps to 750 cps, 750 cps to 800 cps, 800cps to 850 cps, 850 cps to 900 cps, 900 cps to 950 cps, 950 cps to 1000cps, 1,000 cps to 1,250 cps, 1,250 cps to 1,500 cps, 1,500 cps to 1,750cps, 1,750 cps to 2,000 cps, 2,000 cps to 2,500 cps, 2,500 cps to 3,000cps, 3,000 cps to 3,500 cps, 3,500 cps to 4,000 cps, 4,000 cps to 4,500cps, 4,500 cps to 5,000 cps, 5,000 cps to 5,500 cps, 5,500 cps to 6,000cps, 6,000 cps to 6,500 cps, 6,500 cps to 7,000 cps, 7,000 cps to 7,500cps, 7,500 cps to 8,000 cps, 8,000 cps to 8,500 cps, 8,500 cps to 9,000cps, 9,000 cps to 9,500 cps, 9,500 cps to 10,000 cps, 10,000 cps to11,000 cps, 11,000 cps to 12,000 cps, 12,000 cps to 13,000 cps, 13,000cps to 14,000 cps, 14,000 cps to 15,000 cps, 15,000 cps to 16,000 cps,16,000 cps to 17,000 cps, 17,000 cps to 18,000 cps, 18,000 cps to 19,000cps, 19,000 cps to 20,000 cps, 20,000 cps to 21,000 cps, 21,000 cps to22,000 cps, 22,000 cps to 23,000 cps, 23,000 cps to 24,000 cps, 24,000cps to 25,000 cps, and 25,000 cps to 26,000 cps.

(iii) a specific gravity ranging from one or more selected from thegroup consisting of 0.7 to 0.705, 0.705 to 0.71, 0.71 to 0.715, 0.715 to0.72, 0.72 to 0.725, 0.725 to 0.73, 0.73 to 0.735, 0.735 to 0.74, 0.74to 0.745, 0.745 to 0.75, 0.75 to 0.755, 0.755 to 0.76, 0.76 to 0.765,0.765 to 0.77, 0.77 to 0.775, 0.775 to 0.78, 0.78 to 0.785, 0.785 to0.79, 0.79 to 0.795, 0.795 to 0.8, 0.8 to 0.805, 0.805 to 0.81, 0.81 to0.815, 0.815 to 0.82, 0.82 to 0.825, 0.825 to 0.83, 0.83 to 0.835, 0.835to 0.84, 0.84 to 0.845, 0.845 to 0.85, 0.85 to 0.855, 0.855 to 0.86,0.86 to 0.865, 0.865 to 0.87, 0.87 to 0.875, 0.875 to 0.88, 0.88 to0.885, 0.885 to 0.89, 0.89 to 0.895, 0.895 to 0.9, 0.9 to 0.905, 0.905to 0.91, 0.91 to 0.915, 0.915 to 0.92, 0.92 to 0.925, 0.925 to 0.93,0.93 to 0.935, 0.935 to 0.94, 0.94 to 0.945, 0.945 to 0.95, 0.95 to0.955, 0.955 to 0.96, 0.96 to 0.965, 0.965 to 0.97, 0.97 to 0.975, 0.975to 0.98, 0.98 to 0.985, 0.985 to 0.99, 0.99 to 0.995, 0.995 to 0.999,0.999 to 1, 1 to 1.1, 1.1 to 1.2, and 1.2 to 1.3.

(iv) a conductivity ranging from one or more selected from the groupconsisting of 1.00 microsiemens (μS) to 1.25 μS, 1.25 μS to 1.50 μS,1.50 μS to 1.75 μS, 1.75 μS to 2.00 μS, 2.00 μS to 2.25 μS, 2.25 μS to2.50 μS, 2.50 μS to 2.75 μS, 2.75 μS to 3.00 μS, 3.00 μS to 3.25 μS,3.25 μS to 3.50 μS, 3.50 μS to 3.75 μS, 3.75 μS to 4.00 μS, 4.00 μS to4.25 μS, 4.25 μS to 4.50 μS, 4.50 μS to 4.75 μS, 4.75 μS to 5.00 μS,5.00 μS to 5.25 μS, 5.25 μS to 5.50 μS, 5.50 μS to 5.75 μS, 5.75 μS to6.00 μS, 6.00 μS to 6.25 μS, 6.25 μS to 6.50 μS, 6.50 μS, to 6.75 μS,6.75 μS to 7.00 μS, 7.00 μS to 7.25 μS, 7.25 μS to 7.50 μS, 7.50 μS to7.75 μS, 7.75 μS to 8.00 μS, 8.00 μS to 8.25 μS, 8.25 μS to 8.50 μS,8.50 μS to 8.75 μS, 8.75 μS to 9.00 μS, 9.00 μS to 9.25 μS, 9.25 μS to9.50 μS, 9.50 μS to 9.75 μS, 9.75 μS to 10.00 μS, 10.00 μS to 12.50 μS,12.50 μS to 15.00 μS, 15.00 μS to 17.50 μS, 17.50 μS to 20.00 μS, 20.00μS to 22.50 μS, 22.50 μS to 25.00 μS, 25.00 μS to 27.50 μS, 27.50 μS to30.00 μS, 30.00 μS to 32.50 μS, 32.50 μS to 35.00 μS, 35.00 μS to 37.50μS, 37.50 μS to 40.00 μS, 40.00 μS to 42.50 μS, 42.50 μS to 45.00 μS,45.00 μS to 47.50 μS, 47.50 μS to 50.00 μS, 50.00 μS to 52.50 μS, 52.50μS to 55.00 μS, 55.00 μS to 57.50 μS, 57.50 μS to 60.00 μS, 60.00 μS to62.50 μS, 62.50 μS to 65.00 μS, 65.00 μS to 67.50 μS, 67.500 to 70.00μS, 70.000 to 72.50 μS, 72.500 to 75.00 μS, 75.000 to 77.50 μS, and77.50 μS to 80.00 μS. In embodiments, μS means μS per centimeter.

(v) a conductivity ranging from one or more selected from the groupconsisting of 80 μS to 125 μS, 100 μS to 125 μS, 125 μS to 150 μS, 150μS to 175 μS, 175 μS to 200 μS, 200 μS to 225 μS, 225 μS to 250 μS, 250μS to 275 μS, 275 μS to 300 μS, 300 μS to 325 μS, 325 μS to 350 μS, 350μS to 375 μS, 375 μS to 400 μS, 400 μS to 425 μS, 425 μS to 450 μS, 450μS to 475 μS, 475 μS to 500 μS, 500 μS to 525 μS, 525 μS to 550 μS, 550μS to 575 μS, 575 μS to 600 μS, 600 μS to 625 μS, 625 μS to 650 μS, 650μS to 675 μS, 675 μS to 700 μS, 700 μS to 725 μS, 725 μS to 750 μS, 750μS to 775 μS, 775 μS to 800 μS, 800 μS to 825 μS, 825 μS to 850 μS, 850μS to 875 μS, 875 μS to 900 μS, 900 μS to 925 μS, 925 μS to 950 μS, 950μS to 975 μS, 975 μS to 1,000 μS, 1,000 μS to 1,250 μS, 1,250 μS to1,500 μS, 1,500 μS to 1,750 μS, 1,750 μS to 2,000 μS, 2,000 μS to 2,250μS, 2,250 μS to 2,500 μS, 2,500 μS to 2,750 μS, 2,750 μS to 3,000 μS,3,000 μS to 3,250 μS, 3,250 μS to 3,500 μS, 3,500 μS to 3,750 μS, 3,750μS to 4,000 μS, 4,000 μS to 4,250 μS, 4,250 μS to 4,500 μS, 4,500 μS to4,750 μS, 4,750 μS to 5,000 μS, 5,000 μS to 5,250 μS, 5,250 μS to 5,500μS, 5,500 μS to 5,750 μS, 5,750 μS to 6,000 μS, 6,000 μS to 6,250 μS,6,250 μS to 6,500 μS, 6,500 μS to 6,750 μS, 6,750 μS to 7,000 μS, 7,000μS to 7,250 μS, 7,250 μS to 7,500 μS, 7,500 μS to 7,750 and 7,750 μS to8,000 μS In embodiments, μS means μS per centimeter

(vi) a preservation that includes: freezer, 0 degrees F. to 32 degreesF., 30 months to 40 months; refrigerator, 34 degrees F. to 45 degreesF., 30 months to 40 months; elevated temperature, 76 degrees F. to 98degrees F., 4 months to 6 months; ambient temperature, 68 degrees F. to76 degrees F., 30 months to 40 months.

Applicant has discovered an improved process to emulsify a lipophilicand hydrophobic cannabinoid mixture or extract with water. Applicant hasdiscovered an improved process to emulsify a lipophilic and hydrophobiccannabinoid extract with water. The simulated moving bed extractionmethod utilized with an emulsification procedure is a core concept ofthis disclosure shown in FIGS. 17G′ and 17H′.

Lipophilic and hydrophobic cannabinoid mixtures do not easily disperseinto water-based formulations. In embodiments, ultrasonic homogenizerscan be used to produce stable nano-emulsions of cannabinoids in water orany aqueous phase. In embodiments, an emulsification system may be usedfor the production of cannabis oil-emulsions. In embodiments, the typeof emulsification system varies. In embodiments, the type ofemulsification system includes a homogenizer, agitator, sawtooth blade,closed rotor, rotor/stator, an ultrasonic homogenizer rotor/statorgenerator, colloid mill, high pressure, piston pump, a microfluidizer,and a microfluidizer processor.

Applicant has discovered a new microemulsion and nanoemulsion technologybased water soluble platform to greatly enhance the bioavailability ofwater soluble cannabinoid (THC, CBD, etc.) powders, liquids, gels, andcreams. In embodiments, the bioavailability of the cannabinoid emulsionis the proportion of the cannabinoid that enters the circulation of thehuman or animal when introduced into the body and so is able to have anactive effect.

In embodiments, the bioavailability of the cannabinoid emulsion is theproportion of the cannabinoid that enters the circulation of the humanor animal when introduced into the human or animal body and so is ableto have an active effect. In embodiments, the bioavailability of thecannabinoid emulsion is selected from one or more bioavailability rangesselected from one or more from the group of bioavailability rangesconsisting of: 30.00 percent to 40.00 percent, 40.00 percent to 50.00percent, 50.00 percent to 60.00 percent, 60.00 percent to 70.00 percent,70.00 percent to 72.50 percent, 72.50 percent to 75.00 percent, 75.00percent to 77.50 percent, 77.50 percent to 80.00 percent, 80.00 percentto 82.50 percent, 82.50 percent to 85.00 percent, 85.00 percent to 87.50percent, 87.50 percent to 90.00 percent, 90.00 percent to 90.50 percent,90.50 percent to 91.00 percent, 91.00 percent to 91.50 percent, 91.50percent to 92.00 percent, 92.00 percent to 92.50 percent, 92.50 percentto 93.00 percent, 93.00 percent to 93.50 percent, 93.50 percent to 94.00percent, 94.00 percent to 94.50 percent, 94.50 percent to 95.00 percent,95.00 percent to 95.50 percent, 95.50 percent to 96.00 percent, 96.00percent to 96.50 percent, 96.50 percent to 97.00 percent, 97.00 percentto 97.50 percent, 97.50 percent to 98.00 percent, 98.00 percent to 98.50percent, 98.50 percent to 99.00 percent, 99.00 percent to 99.50 percent,and 99.50 percent to 100.00 percent.

In embodiments, these new and advanced water soluble technologyformulations transforms cannabinoid oil (THC, CBD, etc.) intomicroemulsions and nanoemulsions making them more absorbable whendelivered orally, and much more permeable when administered topically.Applicant has discovered a method to make new water soluble powder andliquid cannabinoid drugs, foodstuffs, oils, crystals, and emulsions.

In embodiments, the emulsion is a nano-size emulsion or a nanoemulsionand has nano-size droplets. In embodiments, the emulsion is a micro-sizeemulsion or a microemulsion and has micro-sized droplets. Inembodiments, emulsions, such as micro-sized or nano-sized emulsions, maybe liquids, gels, of creams. In embodiments, emulsions, such asmicro-sized or nano-sized emulsions, may be two immiscible fluidsdispersed into one another. In embodiments, the emulsion containscannabinoids and water. In embodiments, the emulsion containscannabinoids and a solvent.

In embodiments, the emulsion contains cannabinoids, a solvent, anemulsifier, a biocatalyst, and acid. In embodiments, the emulsioncontains cannabinoids, a solvent, an emulsifier, a biocatalyst, anacid/caustic, and water. In embodiments, the emulsion containscannabinoids, a water, an emulsifier, a biocatalyst, drugs, and an acid.In embodiments, the emulsion contains cannabinoids, a water, anemulsifier, a biocatalyst, drugs, an acid/caustic, and a pH adjustmentsolution. In embodiments, the emulsion contains cannabinoids and water.In embodiments, the emulsion contains cannabinoids and deionized water.In embodiments, the emulsion contains cannabinoids and deionized andmembrane treated water. In embodiments, the emulsion containscannabinoids and filtered and deionized water. In embodiments, theemulsion contains cannabinoids and distilled water. In embodiments, theemulsion contains cannabinoids and deionized, membrane treated, anddistilled water. In embodiments, the emulsion contains cannabinoids andfiltered, deionized, and distilled water. In embodiments, the emulsionhas an average droplet size selected from one or more from the groupconsisting of between: 1 nanometers to 2 nanometers, 2 nanometers to 3nanometers, 3 nanometers to 4 nanometers, 4 nanometers to 5 nanometers,5 nanometers to 6 nanometers, 6 nanometers to 7 nanometers, 7 nanometersto 8 nanometers, 8 nanometers to 9 nanometers, 9 nanometers to 10nanometers, 10 nanometers to 11 nanometers, 11 nanometers to 12nanometers, 12 nanometers to 13 nanometers, 13 nanometers to 14nanometers, 14 nanometers to 15 nanometers, 15 nanometers to 16nanometers, 16 nanometers to 17 nanometers, 17 nanometers to 18nanometers, 18 nanometers to 19 nanometers, 19 nanometers to 20nanometers, 20 nanometers to 21 nanometers, 21 nanometers to 22nanometers, 22 nanometers to 23 nanometers, 23 nanometers to 24nanometers, 24 nanometers to 25 nanometers, 25 nanometers to 26nanometers, 26 nanometers to 27 nanometers, 27 nanometers to 28nanometers, 28 nanometers to 29 nanometers, 29 nanometers to 30nanometers, 30 nanometers to 31 nanometers, 31 nanometers to 32nanometers, 32 nanometers to 33 nanometers, 33 nanometers to 34nanometers, 34 nanometers to 35 nanometers, 35 nanometers to 36nanometers, 36 nanometers to 37 nanometers, 37 nanometers to 38nanometers, 38 nanometers to 39 nanometers, 39 nanometers to 40nanometers, 40 nanometers to 41 nanometers, 41 nanometers to 42nanometers, 42 nanometers to 43 nanometers, 43 nanometers to 44nanometers, 44 nanometers to 45 nanometers, 45 nanometers to 46nanometers, 46 nanometers to 47 nanometers, 47 nanometers to 48nanometers, 48 nanometers to 49 nanometers, 49 nanometers to 50nanometers, 50 nanometers to 75 nanometers, 75 nanometers to 100nanometers, 100 nanometers to 150 nanometers, 150 nanometers to 250nanometers, 250 nanometers to 500 nanometers, 500 nanometers to 750nanometers, 750 nanometers to 1,000 nanometers, 1,000 nanometers to1,500 nanometers, 1,500 nanometers to 2,000 nanometers, 2,000 nanometersto 3,000 nanometers, 3,000 nanometers to 4,000 nanometers, 4,000nanometers to 5,000 nanometers, 5,000 nanometers to 6,000 nanometers,and 6,000 nanometers to 10,000 nanometers.

Applicant has discovered new and improved oil-in-water emulsions. Inembodiments, the emulsion is prepared by mixing the cannabinoid andsolvent mixture with an emulsifier. In embodiments, the emulsifier usedin Applicants cannabinoid emulsion process is selected from one or moreemulsifiers selected from the group consisting of a surfactant, anonionic surfactant, lecithin, polyethylene (40), stearate, polysorbate,Polyoxyethylene sorbitan monooleate, Polyoxyethylene (20) sorbitanmonooleate, polysorbate 80, polysorbate 60, polysorbate 65, ammoniumsalts of phosphatidic acid, sucrose acetate isobutyrate, potassiumpyrophosphate, sodium acid pyrophosphate, sodium pyrophosphate,potassium polymetaphosphate, sodium metaphosphate, insoluble or sodiumpolyphosphates, sodium polyphosphates, insoluble polyphosphates, glassysalts of fatty acids, mono- and di-glycerides of fatty acids,mono-glycerides of fatty acids, di-glycerides of fatty acids, acetic andfatty acid esters of glycerol, lactic and fatty acid esters of glycerol,citric and fatty acid esters of glycerol, diacetyltartaric and fattyacid esters of glycerol, mixed fatty acid esters of glycerol, sucroseesters of fatty acids, polyglycerol esters of fatty acids, polyglycerolesters of interesterified ricinoleic acid, propylene glycol mono- anddi-esters, propylene glycol di-esters, propylene glycol mono-esters,propylene glycol esters of fatty acids, propylene glycol esters, dioctylsodium sulphosuccinate, sodium lactylate, sodium oleyl lactylate, sodiumstearoyl lactylate, calcium lactylate, calcium oleyl lactylate, calciumstearoyl lactylate, sorbitan monostearate, maltodextrin, polyphosphates,formulated polyphosphates, and gum arabic.

In embodiment, the biocatalyst includes one or more selected from thegroup consisting of a microorganism, bacteria, fungi, Lactobacilli,Lactobacillus acidophilus, Lactobacillus bulgaricus, Lactobacillusplantarum, Lactobacillus rhamnosus, Lactobacillus fermentum,Lactobacillus caucasicus, Lactobacillus helveticus, Lactobacilluslactis, Lactobacillus reuteri, Lactobacillus casei, Lactobacillusbrevis, Lactobacillus gasseri, Lactobacillus paracasei, Lactobacillussalivarius, Bifidobacteria, Bifidobacterium animalis, Bifidobacteriumbifidum, Bifidobacterium breve, Bifidobacterium infantis,Bifidobacterium lactis, Bifidobacterium longum, Enterococcus faecium,Streptococcus thermophilus, Bacillus laterosporus, and Pediococcusacidilactici.

In embodiments, the drugs include one or more selected from the groupconsisting of a ayahuasca, biologically active organic compound withfour rings, a nootropic drug, acetate, activated charcoal, anamphetamine, ascorbic acid, aspirin, butyrate, calcium, capsaicin,carnitine, carnosine, cassia cinnamon, chondroitin sulfate, chromium,coenzyme q-10, cannabinoids, cannabinoid drugs, water soluble powdercannabinoid drugs, liquid cannabinoid drugs, cranberry, creatine,curcumin, deprenyl, dimethyltryptamine, echinacea, fish oil, garlic,ginger, ginkgo, ginseng, gluconic acid, glucosamine, green tea, hoodia,human growth hormone, 7-hydroxymitragynine, inositol, iowaska, kratom,lactic acid, lithium, lion's mane mushroom, lutein, magnesium, minerals,malate, melatonin, metformin, 3,4-methylenedioxymethamphetamine, milkthistle, n-acetylcysteine, niacin, niacinamide, nicotinamide riboside,omega-3 fatty acid, oxaloacetate, piracetam, psilocybin, pyruvate,resveratrol, rhodiola, saw palmetto, selenium, St. john's wort, steroidalternatives, steroids, testosterone, theaflavins, turmeric, valerian,vitamins, vitamin B3, vitamin C, and zinc.

In embodiments, the drugs include one or more selected from the groupconsisting of basil, bergamot, black pepper, cassia, cedarwood,cinnamon, citronella, clary sage, clove, coffee, cypress, eucalyptus,evening primrose, fennel, fir needle, frankincense, gardenia, geranium,ginger, grapefruit, helichrysum, hop, hyssop, jasmine, juniper berry,lavender, lemon, lemongrass, mandarin, marjoram, melaleuca, melissa,myrrh, neroli, orange, oregano, palo santo, patchouli, peppermint, pine,roman chamomile, rose, rosemary, sandalwood, spikenard, tea tree, thyme,turmeric, vetiver, wintergreen, and ylang ylang.

In embodiments, the drugs include one or more selected from the groupconsisting of barley, binding agents, brown rice, buckwheat flour,buckwheat, bulgur, carrageenan, corn meal, corn, cracked wheat, cricketflour, density improving textural supplements, farro, fiber-starchmaterials, insect flour, insects, mealworms, millet, moisture improvingtextural supplements, oatmeal, popcorn, quinoa, rice, rye, sorghum,triticale, wheat, whole farro, whole grain barley, whole grain corn,whole oats, whole rye, whole wheat flour, wild rice, fiber-starchmaterials, binding agents, density improving textural supplements, andmoisture improving textural supplements.

In embodiments, the emulsion may be further processed to createfoodstuffs not only including ada, bagels, baked goods, biscuits,bitterballen, bonda, breads, cakes, candies, cereals, chips, chocolatebars, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crêpes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, poffertjes, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,specialty milk, tele-bhaja, tempura, toffee, tortillas, totopo, turkishdelights, or waffles.

In embodiments, the fiber-starch materials may be comprised of singularor mixtures of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, or vegetable-based materials. In embodiments, thebinding agents may be comprised of singular or mixtures of agar, agave,alginin, aspartame, arrowroot, carrageenan, collagen, cornstarch, eggwhites, finely ground seeds, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, proteins,psyllium husks, sago, sugars, stevia, syrups, tapioca, vegetable gums,or xanthan gum. In embodiments, the moisture improving texturalsupplements may be comprised of singular or mixtures of almonds, brazilnuts, cacao, cashews, chestnuts, coconut, filberts, hazelnuts, Indiannuts, macadamia nuts, nut butters, nut oils, nut powders, peanuts,pecans, pili nuts, pine nuts, pinon nuts, pistachios, soy nuts,sunflower seeds, tiger nuts, walnuts, and oils extracted from any one ofthe aforesaid nuts and nuts listed herein and combinations thereof. Inembodiments, the insects may be Orthoptera order of insects includinggrasshoppers, crickets, cave crickets, Jerusalem crickets, katydids,weta, lubber, acrida, and locusts. However, other orders of insects,such as cicadas, ants, mealworms, agave worms, worms, bees, centipedes,cockroaches, dragonflies, beetles, scorpions, tarantulas, termites,insect lipids, and insect oil, or any insects or insect productsmentioned herein may be used as well.

In embodiments the emulsion is created in a continuously stirred tankreactor. In embodiments the emulsion is created in a homogenizer. Inembodiments, the emulsion is created using ultrasound technology. Inembodiments, the emulsion is created using ultrasonic homogenizer. Inembodiments, the ultrasonic homogenizer includes an ultrasonic horn(also known as acoustic horn, sonotrode, acoustic waveguide, ultrasonicprobe) is a tapering metal bar commonly used for augmenting theoscillation displacement amplitude provided by an ultrasonic transduceroperating at the low end of the ultrasonic frequency spectrum. Inembodiments, the ultrasonic homogenizer includes one or more ultrasonichomogenizers selected from the group consisting of an ultrasonic horn, aconverging ultrasonic horn, and a barbell ultrasonic horn. Inembodiments, a sonotrode is a tool that creates ultrasonic vibrationsand applies this vibrational energy to a gas, liquid, solid or tissue.In embodiments, a sonotrode includes of a plurality of piezoelectrictransducers attached to a tapering metal rod.

In embodiments, the ultrasonic homogenizer consumes power at a powerconsumption level ranging from one or more power consumption levelsselected from the group consisting of 0.1 kw to 0.25 kw, 0.25 kw to 0.5kw, 0.5 kw to 1 kw, 1 kw to 2 kw, 2 kw to 3 kw, 3 kw to 4 kw, 4 kw to 5kw, 5 kw to 6 kw, 6 kw to 7 kw, 7 kw to 8 kw, 8 kw to 9 kw, 9 kw to 10kw, 10 kw to 11 kw, 11 kw to 12 kw, 12 kw to 13 kw, 13 kw to 14 kw, 14kw to 15 kw, 15 kw to 16 kw, 16 kw to 17 kw, 17 kw to 18 kw, 18 kw to 19kw, 19 kw to 20 kw, 20 kw to 25 kw, 25 kw to 30 kw, 30 kw to 35 kw, 35kw to 40 kw, 40 kw to 45 kw, 45 kw to 50 kw, 50 kw to 55 kw, 55 kw to 60kw, 60 kw to 65 kw, 65 kw to 70 kw, 70 kw to 75 kw, 75 kw to 80 kw, 80kw to 85 kw, 85 kw to 90 kw, 90 kw to 95 kw, 95 kw to 100 kw, 100 kw to300 kw, 300 kw to 500 kw, and 500 kw to 1,000 kw.

In embodiments, the weight percent of emulsifier in the final emulsionproduct includes at least one emulsifier weight percent range that isselected from the emulsifier weight percent ranges selected from thegroup consisting of: 1 weight percent to 2 weight percent, 2 weightpercent to 3 weight percent, 3 weight percent to 4 weight percent, 4weight percent to 5 weight percent, 5 weight percent to 6 weightpercent, 6 weight percent to 7 weight percent, 7 weight percent to 8weight percent, 8 weight percent to 9 weight percent, 9 weight percentto 10 weight percent, 10 weight percent to 11 weight percent, 11 weightpercent to 12 weight percent, 12 weight percent to 13 weight percent, 13weight percent to 14 weight percent, 14 weight percent to 15 weightpercent, 15 weight percent to 16 weight percent, 16 weight percent to 17weight percent, 17 weight percent to 18 weight percent, 18 weightpercent to 19 weight percent, 19 weight percent to 20 weight percent, 20weight percent to 21 weight percent, 21 weight percent to 22 weightpercent, 22 weight percent to 23 weight percent, 23 weight percent to 24weight percent, 24 weight percent to 25 weight percent, 25 weightpercent to 26 weight percent, 26 weight percent to 27 weight percent, 27weight percent to 28 weight percent, 28 weight percent to 29 weightpercent, 29 weight percent to 30 weight percent, 30 weight percent to 31weight percent, 31 weight percent to 32 weight percent, 32 weightpercent to 33 weight percent, 33 weight percent to 34 weight percent, 34weight percent to 35 weight percent, 35 weight percent to 36 weightpercent, 36 weight percent to 37 weight percent, 37 weight percent to 38weight percent, 38 weight percent to 39 weight percent, 39 weightpercent to 40 weight percent, 40 weight percent to 41 weight percent, 41weight percent to 42 weight percent, 42 weight percent to 43 weightpercent, 43 weight percent to 44 weight percent, 44 weight percent to 45weight percent, 45 weight percent to 46 weight percent, 46 weightpercent to 47 weight percent, 47 weight percent to 48 weight percent, 48weight percent to 49 weight percent, 49 weight percent to 50 weightpercent, 50 weight percent to 51 weight percent, 51 weight percent to 52weight percent, 52 weight percent to 53 weight percent, 53 weightpercent to 54 weight percent, 54 weight percent to 55 weight percent, 55weight percent to 56 weight percent, 56 weight percent to 57 weightpercent, 57 weight percent to 58 weight percent, 58 weight percent to 59weight percent, 59 weight percent to 60 weight percent, 60 weightpercent to 61 weight percent, 61 weight percent to 62 weight percent, 62weight percent to 63 weight percent, 63 weight percent to 64 weightpercent, 64 weight percent to 65 weight percent, and 65 weight percentto 66 weight percent.

In embodiments, the weight percent of cannabinoids in the final emulsionproduct includes at least one cannabinoid weight percent range that isselected from the cannabinoid weight percent ranges selected from thegroup consisting of: 1 weight percent to 2 weight percent, 2 weightpercent to 3 weight percent, 3 weight percent to 4 weight percent, 4weight percent to 5 weight percent, 5 weight percent to 6 weightpercent, 6 weight percent to 7 weight percent, 7 weight percent to 8weight percent, 8 weight percent to 9 weight percent, 9 weight percentto 10 weight percent, 10 weight percent to 11 weight percent, 11 weightpercent to 12 weight percent, 12 weight percent to 13 weight percent, 13weight percent to 14 weight percent, 14 weight percent to 15 weightpercent, 15 weight percent to 16 weight percent, 16 weight percent to 17weight percent, 17 weight percent to 18 weight percent, 18 weightpercent to 19 weight percent, 19 weight percent to 20 weight percent, 20weight percent to 21 weight percent, 21 weight percent to 22 weightpercent, 22 weight percent to 23 weight percent, 23 weight percent to 24weight percent, 24 weight percent to 25 weight percent, 25 weightpercent to 26 weight percent, 26 weight percent to 27 weight percent, 27weight percent to 28 weight percent, 28 weight percent to 29 weightpercent, 29 weight percent to 30 weight percent, 30 weight percent to 31weight percent, 31 weight percent to 32 weight percent, 32 weightpercent to 33 weight percent, 33 weight percent to 34 weight percent, 34weight percent to 35 weight percent, 35 weight percent to 36 weightpercent, 36 weight percent to 37 weight percent, 37 weight percent to 38weight percent, 38 weight percent to 39 weight percent, 39 weightpercent to 40 weight percent, 40 weight percent to 41 weight percent, 41weight percent to 42 weight percent, 42 weight percent to 43 weightpercent, 43 weight percent to 44 weight percent, 44 weight percent to 45weight percent, 45 weight percent to 46 weight percent, 46 weightpercent to 47 weight percent, 47 weight percent to 48 weight percent, 48weight percent to 49 weight percent, 49 weight percent to 50 weightpercent, 50 weight percent to 51 weight percent, 51 weight percent to 52weight percent, 52 weight percent to 53 weight percent, 53 weightpercent to 54 weight percent, 54 weight percent to 55 weight percent, 55weight percent to 56 weight percent, 56 weight percent to 57 weightpercent, 57 weight percent to 58 weight percent, 58 weight percent to 59weight percent, 59 weight percent to 60 weight percent, 60 weightpercent to 61 weight percent, 61 weight percent to 62 weight percent, 62weight percent to 63 weight percent, 63 weight percent to 64 weightpercent, 64 weight percent to 65 weight percent, and 65 weight percentto 66 weight percent.

In embodiments, the weight percent of acid in the final emulsion productincludes at least one acid weight percent range that is selected fromthe acid weight percent ranges selected from the group consisting of: 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, 14 weight percent to 15 weight percent, 15 weightpercent to 16 weight percent, 16 weight percent to 17 weight percent, 17weight percent to 18 weight percent, 18 weight percent to 19 weightpercent, 19 weight percent to 20 weight percent, 20 weight percent to 21weight percent, 21 weight percent to 22 weight percent, 22 weightpercent to 23 weight percent, 23 weight percent to 24 weight percent, 24weight percent to 25 weight percent, 25 weight percent to 26 weightpercent, 26 weight percent to 27 weight percent, 27 weight percent to 28weight percent, 28 weight percent to 29 weight percent, 29 weightpercent to 30 weight percent, 30 weight percent to 31 weight percent, 31weight percent to 32 weight percent, 32 weight percent to 33 weightpercent, 33 weight percent to 34 weight percent, 34 weight percent to 35weight percent, 35 weight percent to 36 weight percent, 36 weightpercent to 37 weight percent, 37 weight percent to 38 weight percent, 38weight percent to 39 weight percent, 39 weight percent to 40 weightpercent, 40 weight percent to 41 weight percent, 41 weight percent to 42weight percent, 42 weight percent to 43 weight percent, 43 weightpercent to 44 weight percent, 44 weight percent to 45 weight percent, 45weight percent to 46 weight percent, 46 weight percent to 47 weightpercent, 47 weight percent to 48 weight percent, 48 weight percent to 49weight percent, 49 weight percent to 50 weight percent, 50 weightpercent to 51 weight percent, 51 weight percent to 52 weight percent, 52weight percent to 53 weight percent, 53 weight percent to 54 weightpercent, 54 weight percent to 55 weight percent, 55 weight percent to 56weight percent, 56 weight percent to 57 weight percent, 57 weightpercent to 58 weight percent, 58 weight percent to 59 weight percent, 59weight percent to 60 weight percent, 60 weight percent to 61 weightpercent, 61 weight percent to 62 weight percent, 62 weight percent to 63weight percent, 63 weight percent to 64 weight percent, 64 weightpercent to 65 weight percent, and 65 weight percent to 66 weightpercent.

In embodiments, the weight percent of biocatalyst in the final emulsionproduct includes at least one biocatalyst weight percent range that isselected from the biocatalyst weight percent ranges selected from thegroup consisting of: 25 parts per million to 0.1 weight percent, 0.1weight percent to 0.5 weight percent, 0.5 weight percent to 1 weightpercent, 1 weight percent to 2 weight percent, 2 weight percent to 3weight percent, 3 weight percent to 4 weight percent, 4 weight percentto 5 weight percent, 5 weight percent to 6 weight percent, 6 weightpercent to 7 weight percent, 7 weight percent to 8 weight percent, 8weight percent to 9 weight percent, 9 weight percent to 10 weightpercent, 10 weight percent to 11 weight percent, 11 weight percent to 12weight percent, 12 weight percent to 13 weight percent, 13 weightpercent to 14 weight percent, 14 weight percent to 15 weight percent, 15weight percent to 16 weight percent, 16 weight percent to 17 weightpercent, 17 weight percent to 18 weight percent, 18 weight percent to 19weight percent, 19 weight percent to 20 weight percent, 20 weightpercent to 21 weight percent, 21 weight percent to 22 weight percent, 22weight percent to 23 weight percent, 23 weight percent to 24 weightpercent, 24 weight percent to 25 weight percent, 25 weight percent to 26weight percent, 26 weight percent to 27 weight percent, 27 weightpercent to 28 weight percent, 28 weight percent to 29 weight percent, 29weight percent to 30 weight percent, 30 weight percent to 31 weightpercent, 31 weight percent to 32 weight percent, 32 weight percent to 33weight percent, 33 weight percent to 34 weight percent, 34 weightpercent to 35 weight percent, 35 weight percent to 36 weight percent, 36weight percent to 37 weight percent, 37 weight percent to 38 weightpercent, 38 weight percent to 39 weight percent, 39 weight percent to 40weight percent, 40 weight percent to 41 weight percent, 41 weightpercent to 42 weight percent, 42 weight percent to 43 weight percent, 43weight percent to 44 weight percent, 44 weight percent to 45 weightpercent, 45 weight percent to 46 weight percent, 46 weight percent to 47weight percent, 47 weight percent to 48 weight percent, 48 weightpercent to 49 weight percent, 49 weight percent to 50 weight percent, 50weight percent to 51 weight percent, 51 weight percent to 52 weightpercent, 52 weight percent to 53 weight percent, 53 weight percent to 54weight percent, 54 weight percent to 55 weight percent, 55 weightpercent to 56 weight percent, 56 weight percent to 57 weight percent, 57weight percent to 58 weight percent, 58 weight percent to 59 weightpercent, 59 weight percent to 60 weight percent, 60 weight percent to 61weight percent, 61 weight percent to 62 weight percent, 62 weightpercent to 63 weight percent, 63 weight percent to 64 weight percent, 64weight percent to 65 weight percent, and 65 weight percent to 66 weightpercent.

In embodiments, the weight percent of drugs in the final emulsionproduct includes at least one drug weight percent range that is selectedfrom the drug weight percent ranges selected from the group consistingof: 0.001 weight percent to 0.002 weight percent, 0.002 weight percentto 0.01 weight percent, 0.01 weight percent to 0.1 weight percent, 0.1weight percent to 0.5 weight percent, 0.5 weight percent to 0.6 weightpercent, 0.6 weight percent to 0.7 weight percent, 0.7 weight percent to0.8 weight percent, 0.8 weight percent to 0.9 weight percent, 0.9 weightpercent to 1.0 weight percent, 1.0 weight percent to 1.1 weight percent,1.1 weight percent to 1.2 weight percent, 1.2 weight percent to 1.3weight percent, 1.3 weight percent to 1.4 weight percent, 1.4 weightpercent to 1.5 weight percent, 1.5 weight percent to 1.6 weight percent,1.6 weight percent to 1.7 weight percent, 1.7 weight percent to 1.8weight percent, 1.8 weight percent to 1.9 weight percent, 1.9 weightpercent to 2.0 weight percent, 2.0 weight percent to 2.1 weight percent,2.1 weight percent to 2.2 weight percent, 2.2 weight percent to 2.3weight percent, 2.3 weight percent to 2.4 weight percent, 2.4 weightpercent to 2.5 weight percent, 2.5 weight percent to 2.6 weight percent,2.6 weight percent to 2.7 weight percent, 2.7 weight percent to 2.8weight percent, 2.8 weight percent to 2.9 weight percent, 2.9 weightpercent to 3.0 weight percent, 3.0 weight percent to 3.1 weight percent,3.1 weight percent to 3.2 weight percent, 3.2 weight percent to 3.3weight percent, 3.3 weight percent to 3.4 weight percent, 3.4 weightpercent to 3.5 weight percent, 3.5 weight percent to 3.6 weight percent,3.6 weight percent to 3.7 weight percent, 3.7 weight percent to 3.8weight percent, 3.8 weight percent to 3.9 weight percent, 3.9 weightpercent to 4.0 weight percent, 4.0 weight percent to 4.1 weight percent,4.1 weight percent to 4.2 weight percent, 4.2 weight percent to 4.3weight percent, 4.3 weight percent to 4.4 weight percent, 4.4 weightpercent to 4.5 weight percent, 4.5 weight percent to 4.6 weight percent,4.6 weight percent to 4.7 weight percent, 4.7 weight percent to 4.8weight percent, 4.8 weight percent to 4.9 weight percent, 4.9 weightpercent to 5.0 weight percent, 5.0 weight percent to 5.1 weight percent,5.1 weight percent to 5.2 weight percent, 5.2 weight percent to 5.3weight percent, 5.3 weight percent to 5.4 weight percent, 5.4 weightpercent to 5.5 weight percent, 5.5 weight percent to 5.6 weight percent,5.6 weight percent to 5.7 weight percent, 5.7 weight percent to 5.8weight percent, 5.8 weight percent to 5.9 weight percent, 5.9 weightpercent to 6.0 weight percent, 6.0 weight percent to 6.1 weight percent,6.1 weight percent to 6.2 weight percent, 6.2 weight percent to 6.3weight percent, 6.3 weight percent to 6.4 weight percent, 6.4 weightpercent to 6.5 weight percent, and 6.5 weight percent to 6.6 weightpercent.

In embodiments, the weight percent of caustic in the final emulsionproduct includes at least one caustic weight percent range that isselected from the caustic weight percent ranges selected from the groupconsisting of: 1 weight percent to 2 weight percent, 2 weight percent to3 weight percent, 3 weight percent to 4 weight percent, 4 weight percentto 5 weight percent, 5 weight percent to 6 weight percent, 6 weightpercent to 7 weight percent, 7 weight percent to 8 weight percent, 8weight percent to 9 weight percent, 9 weight percent to 10 weightpercent, 10 weight percent to 11 weight percent, 11 weight percent to 12weight percent, 12 weight percent to 13 weight percent, 13 weightpercent to 14 weight percent, 14 weight percent to 15 weight percent, 15weight percent to 16 weight percent, 16 weight percent to 17 weightpercent, 17 weight percent to 18 weight percent, 18 weight percent to 19weight percent, 19 weight percent to 20 weight percent, 20 weightpercent to 21 weight percent, 21 weight percent to 22 weight percent, 22weight percent to 23 weight percent, 23 weight percent to 24 weightpercent, 24 weight percent to 25 weight percent, 25 weight percent to 26weight percent, 26 weight percent to 27 weight percent, 27 weightpercent to 28 weight percent, 28 weight percent to 29 weight percent, 29weight percent to 30 weight percent, 30 weight percent to 31 weightpercent, 31 weight percent to 32 weight percent, and 32 weight percentto 33 weight percent.

In embodiments, the weight percent of water in the final emulsionproduct includes at least one caustic water percent range that isselected from the water weight percent ranges selected from the groupconsisting of: 1 weight percent to 2 weight percent, 2 weight percent to3 weight percent, 3 weight percent to 4 weight percent, 4 weight percentto 5 weight percent, 5 weight percent to 6 weight percent, 6 weightpercent to 7 weight percent, 7 weight percent to 8 weight percent, 8weight percent to 9 weight percent, 9 weight percent to 10 weightpercent, 10 weight percent to 11 weight percent, 11 weight percent to 12weight percent, 12 weight percent to 13 weight percent, 13 weightpercent to 14 weight percent, 14 weight percent to 15 weight percent, 15weight percent to 16 weight percent, 16 weight percent to 17 weightpercent, 17 weight percent to 18 weight percent, 18 weight percent to 19weight percent, 19 weight percent to 20 weight percent, 20 weightpercent to 21 weight percent, 21 weight percent to 22 weight percent, 22weight percent to 23 weight percent, 23 weight percent to 24 weightpercent, 24 weight percent to 25 weight percent, 25 weight percent to 26weight percent, 26 weight percent to 27 weight percent, 27 weightpercent to 28 weight percent, 28 weight percent to 29 weight percent, 29weight percent to 30 weight percent, 30 weight percent to 31 weightpercent, 31 weight percent to 32 weight percent, 32 weight percent to 33weight percent, 33 weight percent to 34 weight percent, 34 weightpercent to 35 weight percent, 35 weight percent to 36 weight percent, 36weight percent to 37 weight percent, 37 weight percent to 38 weightpercent, 38 weight percent to 39 weight percent, 39 weight percent to 40weight percent, 40 weight percent to 41 weight percent, 41 weightpercent to 42 weight percent, 42 weight percent to 43 weight percent, 43weight percent to 44 weight percent, 44 weight percent to 45 weightpercent, 45 weight percent to 46 weight percent, 46 weight percent to 47weight percent, 47 weight percent to 48 weight percent, 48 weightpercent to 49 weight percent, 49 weight percent to 50 weight percent, 50weight percent to 51 weight percent, 51 weight percent to 52 weightpercent, 52 weight percent to 53 weight percent, 53 weight percent to 54weight percent, 54 weight percent to 55 weight percent, 55 weightpercent to 56 weight percent, 56 weight percent to 57 weight percent, 57weight percent to 58 weight percent, 58 weight percent to 59 weightpercent, 59 weight percent to 60 weight percent, 60 weight percent to 61weight percent, 61 weight percent to 62 weight percent, 62 weightpercent to 63 weight percent, 63 weight percent to 64 weight percent, 64weight percent to 65 weight percent, and 65 weight percent to 66 weightpercent.

In embodiments, the weight percent of treated water in the finalemulsion product includes at least one treated water percent range thatis selected from the treated water weight percent ranges selected fromthe group consisting of: 1 weight percent to 2 weight percent, 2 weightpercent to 3 weight percent, 3 weight percent to 4 weight percent, 4weight percent to 5 weight percent, 5 weight percent to 6 weightpercent, 6 weight percent to 7 weight percent, 7 weight percent to 8weight percent, 8 weight percent to 9 weight percent, 9 weight percentto 10 weight percent, 10 weight percent to 11 weight percent, 11 weightpercent to 12 weight percent, 12 weight percent to 13 weight percent, 13weight percent to 14 weight percent, 14 weight percent to 15 weightpercent, 15 weight percent to 16 weight percent, 16 weight percent to 17weight percent, 17 weight percent to 18 weight percent, 18 weightpercent to 19 weight percent, 19 weight percent to 20 weight percent, 20weight percent to 21 weight percent, 21 weight percent to 22 weightpercent, 22 weight percent to 23 weight percent, 23 weight percent to 24weight percent, 24 weight percent to 25 weight percent, 25 weightpercent to 26 weight percent, 26 weight percent to 27 weight percent, 27weight percent to 28 weight percent, 28 weight percent to 29 weightpercent, 29 weight percent to 30 weight percent, 30 weight percent to 31weight percent, 31 weight percent to 32 weight percent, 32 weightpercent to 33 weight percent, 33 weight percent to 34 weight percent, 34weight percent to 35 weight percent, 35 weight percent to 36 weightpercent, 36 weight percent to 37 weight percent, 37 weight percent to 38weight percent, 38 weight percent to 39 weight percent, 39 weightpercent to 40 weight percent, 40 weight percent to 41 weight percent, 41weight percent to 42 weight percent, 42 weight percent to 43 weightpercent, 43 weight percent to 44 weight percent, 44 weight percent to 45weight percent, 45 weight percent to 46 weight percent, 46 weightpercent to 47 weight percent, 47 weight percent to 48 weight percent, 48weight percent to 49 weight percent, 49 weight percent to 50 weightpercent, 50 weight percent to 51 weight percent, 51 weight percent to 52weight percent, 52 weight percent to 53 weight percent, 53 weightpercent to 54 weight percent, 54 weight percent to 55 weight percent, 55weight percent to 56 weight percent, 56 weight percent to 57 weightpercent, 57 weight percent to 58 weight percent, 58 weight percent to 59weight percent, 59 weight percent to 60 weight percent, 60 weightpercent to 61 weight percent, 61 weight percent to 62 weight percent, 62weight percent to 63 weight percent, 63 weight percent to 64 weightpercent, 64 weight percent to 65 weight percent, and 65 weight percentto 66 weight percent, 66 weight percent to 67 weight percent, 67 weightpercent to 68 weight percent, 68 weight percent to 69 weight percent, 69weight percent to 70 weight percent, 70 weight percent to 71 weightpercent, 71 weight percent to 72 weight percent, 72 weight percent to 73weight percent, 73 weight percent to 74 weight percent, 74 weightpercent to 75 weight percent, 75 weight percent to 76 weight percent, 76weight percent to 77 weight percent, 77 weight percent to 78 weightpercent, 78 weight percent to 79 weight percent, 79 weight percent to 80weight percent, 80 weight percent to 81 weight percent, 81 weightpercent to 82 weight percent, 82 weight percent to 83 weight percent, 83weight percent to 84 weight percent, 84 weight percent to 85 weightpercent, 85 weight percent to 86 weight percent, 86 weight percent to 87weight percent, 87 weight percent to 88 weight percent, 88 weightpercent to 89 weight percent, 89 weight percent to 90 weight percent, 90weight percent to 91 weight percent, 91 weight percent to 92 weightpercent, 92 weight percent to 93 weight percent, 93 weight percent to 94weight percent, 94 weight percent to 95 weight percent, 95 weightpercent to 95.50 weight percent, 95.50 weight percent to 96.00 weightpercent, 96.00 weight percent to 96.50 weight percent, 96.50 weightpercent to 97.00 weight percent, 97.00 weight percent to 97.50 weightpercent, 97.50 weight percent to 98.00 weight percent, 98.00 weightpercent to 98.25 weight percent, 98.25 weight percent to 98.50 weightpercent, 98.50 weight percent to 98.75 weight percent, 98.75 weightpercent to 99.00 weight percent, 99.00 weight percent to 99.25 weightpercent, 99.25 weight percent to 99.50 weight percent, 99.50 weightpercent to 99.55 weight percent, 99.55 weight percent to 99.60 weightpercent, 99.60 weight percent to 99.65 weight percent, 99.65 weightpercent to 99.70 weight percent, 99.70 weight percent to 99.75 weightpercent, 99.75 weight percent to 99.80 weight percent, 99.80 weightpercent to 99.85 weight percent, 99.85 weight percent to 99.90 weightpercent, 99.90 weight percent to 99.95 weight percent, 99.950 weightpercent to 99.955 weight percent, 99.955 weight percent to 99.960 weightpercent, 99.960 weight percent to 99.965 weight percent, 99.965 weightpercent to 99.970 weight percent, 99.970 weight percent to 99.975 weightpercent, 99.975 weight percent to 99.980 weight percent, 99.980 weightpercent to 99.985 weight percent, 99.985 weight percent to 99.990 weightpercent, 99.990 weight percent to 99.995 weight percent, 99.995 weightpercent to 99.996 weight percent, 99.996 weight percent to 99.997 weightpercent, 99.997 weight percent to 99.998 weight percent, 99.998 weightpercent to 99.999 weight percent, or 99.999 weight percent to 99.9999weight percent.

In embodiments, a homogenizer may be configured to homogenizecannabinoids, solvents, water, an emulsifier, an acid/caustic, abiocatalyst, drugs, and a caustic material. In embodiments,homogenization may include any number of several processes used to makea mixture of two mutually non-soluble liquids the same throughout. Inembodiments, homogenization is used to create an emulsion. Inembodiments, an emulsification system may be configured to emulsifycannabinoids, solvents, water, an emulsifier, an acid/caustic, abiocatalyst, drugs, insect, and biomass. In embodiments, emulsificationmay include any number of several processes used to make a mixture oftwo mutually non-soluble liquids the same throughout. In embodiments, anemulsification system is used to create an emulsion.

In embodiments, a mixture of cannabinoids, solvents, water, anemulsifier, an acid/caustic, a biocatalyst, and drugs is introduced toan emulsification system at a pressure greater than the emulsion that isdischarged from the emulsifier system. In embodiments, the pressure dropacross the emulsification system is selected from one or more pressuredrop ranges selected from the group consisting of 25 pounds per squareinch (PSI) to 50 PSI, 50 PSI to 100 PSI, 100 PSI to 200 PSI, 200 PSI to300 PSI, 300 PSI to 400 PSI, 400 PSI to 500 PSI, 500 PSI to 600 PSI, 600PSI to 700 PSI, 700 PSI to 800 PSI, 800 PSI to 900 PSI, 900 PSI to 1,000PSI, 1,000 PSI to 1,500 PSI, 1,500 PSI to 2,000 PSI, 2,000 PSI to 2,500PSI, 2,500 PSI to 3,000 PSI, 3,000 PSI to 3,500 PSI, 3,500 PSI to 4,000PSI, 4,000 PSI to 4,500 PSI, 4,500 PSI to 5,000 PSI, 5,000 PSI to 5,500PSI, 5,500 PSI to 6,000 PSI, 6,000 PSI to 6,500 PSI, 6,500 PSI to 7,000PSI, 7,000 PSI to 7,500 PSI, 7,500 PSI to 8,000 PSI, 8,000 PSI to 8,500PSI, 8,500 PSI to 9,000 PSI, 9,000 PSI to 9,500 PSI, 9,500 PSI to 10,000PSI, 10,000 PSI to 11,000 PSI, 11,000 PSI to 12,000 PSI, 12,000 PSI to13,000 PSI, 13,000 PSI to 14,000 PSI, 14,000 PSI to 15,000 PSI, 15,000PSI to 16,000 PSI, 16,000 PSI to 17,000 PSI, 17,000 PSI to 18,000 PSI,18,000 PSI to 19,000 PSI, 19,000 PSI to 20,000 PSI, 20,000 PSI to 22,500PSI, 22,500 PSI to 25,000 PSI, 25,000 PSI to 27,500 PSI, 27,500 PSI to30,000 PSI, 30,000 PSI to 35,000 PSI. and 35,000 PSI to 40,000 PSI.

In embodiments the emulsion is created under inert gas conditions in thepresence of a gas such as and not only including carbon dioxide,nitrogen, or argon. In embodiments, an inert gas is introduced to theemulsion mixing tank to prolong the life of the emulsion product. Thegas supply system is configured to continuously maintain a positivepressure in the vapor space within the emulsion mixing tank.

In embodiments, the beverage includes carbon dioxide. In embodiments,the carbon dioxide is colorless, odorless, nonflammable, has a meltingpoint or sublimination temperature ranging from −120 to −100 degreesFahrenheit, a critical temperature ranging from 70 to 90 degreesFahrenheit, a vapor pressure ranging from 800 to 875 PSIG, a vapordensity ranging from 1.25 to 1.75, a specific volume ranging from 8 to 9ft3/lb, and a gas density ranging from 0.1 to 0.15 lb/ft3.

In embodiments, the beverage includes carbon dioxide solubilitycoefficient. In embodiments, the solubility coefficient is the volume ofcarbon dioxide that can be dissolved by a unit volume of beverage (e.g.treated water) at a specified pressure and temperature. In embodiments,the solubility coefficient the solubility coefficient of carbon dioxidein the water-based beverage is the reciprocal of Henry's law coefficientH. In embodiments, Henry's law coefficient H applies to cannabis-derivedbeverages (or insect-derived beverages, psilocybin beverages,drug-infused beverages, etc.). and is a gas law that states that theamount of dissolved carbon dioxide in water within the beverage isproportional to its partial pressure above the beverage.

In embodiments, solubility of carbon dioxide in the beverage includesone or more solubility coefficient ranges selected from the groupconsisting of 0.50 to 1.00, 1.00 to 1.50, 1.50 to 2.00, 2.00 to 2.50,2.50 to 3.00, 3.00 to 3.50, 3.50 to 4.00, 4.00 to 4.50, 4.50 to 5.00,5.00 to 5.50, 5.50 to 6.00, 6.00 to 6.50, 6.50 to 7.00, 7.00 to 7.50,7.50 to 8.00, 8.00 to 8.50, 8.50 to 9.00, 9.00 to 9.50, 9.50 to 10.00,10.00 to 10.50, 10.50 to 11.00, 11.00 to 11.50, 11.50 to 12.00, 12.00 to12.50, 12.50 to 13.00, 13.00 to 13.50, 13.50 to 14.00, 14.00 to 14.50,and 14.50 to 15.00.

In embodiments, solubility of carbon dioxide in the beverage includesone or more Bunsen coefficient ranges selected from the group consistingof 0.50 to 1.00, 1.00 to 1.50, 1.50 to 2.00, 2.00 to 2.50, 2.50 to 3.00,3.00 to 3.50, 3.50 to 4.00, 4.00 to 4.50, 4.50 to 5.00, 5.00 to 5.50,5.50 to 6.00, 6.00 to 6.50, 6.50 to 7.00, 7.00 to 7.50, 7.50 to 8.00,8.00 to 8.50, 8.50 to 9.00, 9.00 to 9.50, 9.50 to 10.00, 10.00 to 10.50,10.50 to 11.00, 11.00 to 11.50, 11.50 to 12.00, 12.00 to 12.50, 12.50 to13.00, 13.00 to 13.50, 13.50 to 14.00, 14.00 to 14.50, and 14.50 to15.00, wherein: the Bunsen coefficient the number of milliliters of gasdissolved in a milliliter of liquid at atmospheric pressure (760 mm Hg)and a specified temperature.

In embodiments, solubility of carbon dioxide in the beverage isdetermined by the Zahm-Nagel technique which calculates carbon dioxidelevels within the beverages using measurements of headspace of the tankor beverage, partial pressure, and beverage temperature.

In embodiments, solubility of carbon dioxide in the beverage is measuredwith a beverage carbonation tester. In embodiments, the beverages isbottled in a bottle, wherein the bottle is clear, brown, green, or ambercolored. In embodiments, the beverages is bottled in a plastic bottle,wherein the plastic bottle is comprised of polyethylene terephthalate(PET or PETE or Polyester), high-density polyethylene (HDPE), polyvinylchloride (PVC), low-density polyethylene (LDPE), polypropylene (PP),polystyrene (PS). In embodiments, the beverage is bottled in a metalcan, wherein the metal can includes tin, aluminum, or copper, ormixtures of tin and aluminum.

In embodiments, solubility of carbon dioxide in the beverage is measuredwith a variety of instruments provided by Zahm & Nagel Co., Inc. of 210Vermont Street, Holland, N.Y. 14080 USA, which include: the Series 1000carbon dioxide Volume Meter, the Series 6000 Zahm Model D.T. PiercingDevice, the Series 7000 Zahm New Style Air Tester with Dial Thermometer,and the Series 11000 Zahm Modified Piercing Device.

The Series 1000 carbon dioxide Volume Meter (Part #1000D) is used todetermine average carbon dioxide levels of gas in the beverage tank orbottle by using a piston release mechanism. In embodiments, thebeverages is bottled in a glass bottle, wherein the glass bottle isclear, brown, green, or amber colored.

The Series 6000 Zahm Model D.T. Piercing Device (Part #6000) is used totest the carbonated beverage for volumes of carbon dioxide gas inglass/PET bottles and cans; this instrument uses a dual scale pressuregauge (0-60 psi & 0-4.2 kg/cm2) and an adjustable 2″ dial thermometer(25/125° F. & −5/55° C.). It is available in one and three liter sizes.The Series 6000 Piercing Device will provide rapid and accuratedetermination of carbon dioxide gas volumes in beverages describedherein.

The Series 7000 Zahm New Style Air Tester with Dial Thermometer (Part#7000) is used to test beverage or product for carbon dioxide gas andair content in either glass or PET containers and cans. It isautomatically adjustable to various size bottles and cans and isavailable in either one or two liter sizes. This instrument can be usedto determine the headspace “air” within the beverage bottle, wherein theheadspace “air” is defined as atmospheric air picked up during thebrewing or bottling process.

The Series 11000 Zahm Modified Piercing Device (Part #11000) is usedwhen a separately mounted burette is preferred for air testing or wherea fast, simple closure piercing unit is required to measure pressure.Where samples are tested at room or known temperature, gas pressure canbe quickly obtained to determine carbon dioxide gas volumes.

In embodiments, the solubility coefficient affects the type of beverage,stability, shelf-life, packing options, and sensory aspects of thebeverage. In embodiments, the beverage has a shelf life ranging from 2months to 4 months, 4 months to 6 months, 6 months to 8 months, 8 monthsto 10 months, 10 months to 12 months, 12 months to 14 months, 14 monthsto 16 months, 16 months to 18 months, 18 months to 20 months, 20 monthsto 22 months, 22 months to 24 months, 24 months to 26 months, 26 monthsto 28 months, 28 months to 30 months, 30 months to 32 months, 32 monthsto 34 months, 34 months to 36 months, 36 months to 38 months, 38 monthsto 40 months, 40 months to 42 months, 42 months to 44 months, 44 monthsto 46 months, 46 months to 48 months, 48 months to 50 months, 50 monthsto 52 months, 52 months to 54 months, 54 months to 56 months, 56 monthsto 58 months, and 58 months to 60 months. For example, in embodiments,the beverage has a shelf life ranging from 12 months to 24 months. Forexample, in embodiments, the beverage has a shelf life ranging from 18months to 30 months. For example, in embodiments, the beverage has ashelf life ranging from 12 months to 48 months. For example, inembodiments, the beverage has a shelf life ranging from 14 months to 48months.

FIG. 17J′ displays an acid-caustic distribution system (JAA) includingan acid-caustic tank (JAB) that is configured to accept acid-caustic(JAD). The acid-caustic tank (JAB) has an interior (JAC), anacid-caustic input (JAF), an acid-caustic conveyor (JAG), and anacid-caustic conveyor output (JAH). The acid-caustic tank (JAB) acceptsacid and/or caustic (JAD) to the interior (JAC) and regulates andcontrols an engineered amount of acid and/or caustic (JAD) downstream tobe mixed to form an emulsion. The acid-caustic conveyor (6B5) has anintegrated mass sensor (JAJ) that is configured to input and output asignal (JAK) to the computer (COMP). The acid-caustic conveyor motor(JAL) has a controller (JAM) that is configured to input and output asignal (JAN) to the computer (COMP). The mass sensor (JAJ), acid-causticconveyor (JAG), and acid-caustic conveyor motor (JAL) are coupled so asto permit the conveyance, distribution, or output of a precise flow ofacid and/or caustic (JAD) via an acid-caustic transfer line (JAI). It isto be noted that the acid-caustic may be in solid, powder, liquid, orslurry form. Transferring an engineered amount of acid and/or caustic(JAD) downstream to be mixed to form an emulsion is the premise of thedisclosure and is not limited to regulating as a solid, powder, liquid,gel, slurry, or the equivalent.

FIG. 17J′ displays a biocatalyst distribution system (JBA) including abiocatalyst tank (JBB) that is configured to accept a biocatalyst (JBD).The biocatalyst tank (JBB) has an interior (JBC), a biocatalyst input(JBF), a biocatalyst conveyor (JBG), and a biocatalyst conveyor output(JBH). The biocatalyst tank (JBB) accepts a biocatalyst (JBD) to theinterior (JBC) and regulates and controls an engineered amount ofbiocatalyst (JBD) downstream to be mixed to form an emulsion. Thebiocatalyst conveyor (6B5) has an integrated mass sensor (JBJ) that isconfigured to input and output a signal (JBK) to the computer (COMP).The biocatalyst conveyor motor (JBL) has a controller (JBM) that isconfigured to input and output a signal (JBN) to the computer (COMP).The mass sensor (JBJ), biocatalyst conveyor (JBG), and biocatalystconveyor motor (JBL) are coupled so as to permit the conveyance,distribution, or output of a precise flow of biocatalyst (JBD) via abiocatalyst transfer line (JBI). It is to be noted that the biocatalystmay be in solid, powder, liquid, or slurry form. Transferring anengineered amount of biocatalyst (JBD) downstream to be mixed to form anemulsion is the premise of the disclosure and is not limited toregulating as a solid, powder, liquid, gel, slurry, or the equivalent.

FIG. 17J′ displays a drug distribution system (JCA) including a drugtank (JCB) that is configured to accept a drug (JCD). The drug tank(JCB) has an interior (JCC), a drug input (JCF), a drug conveyor (JCG),and a drug conveyor output (JCH). The drug tank (JCB) accepts drugs(JCD) to the interior (JCC) and regulates and controls an engineeredamount of drugs (JCD) downstream to be mixed to form an emulsion. Thedrug conveyor (6B5) has an integrated mass sensor (JCJ) that isconfigured to input and output a signal (JCK) to the computer (COMP).The drug conveyor motor (JCL) has a controller (JCM) that is configuredto input and output a signal (JCN) to the computer (COMP). The masssensor (JCJ), drug conveyor (JCG), and drug conveyor motor (JCL) arecoupled so as to permit the conveyance, distribution, or output of aprecise flow of drugs (JCD) via a drug transfer line (JCI). It is to benoted that the drugs may be in solid, powder, liquid, or slurry form.Transferring an engineered amount of drugs (JCD) downstream to be mixedto form an emulsion is the premise of the disclosure and is not limitedto regulating as a solid, powder, liquid, gel, slurry, or theequivalent.

FIG. 17J′ displays an emulsifier distribution system (JDA) including anemulsifier tank (JDB) that is configured to accept an emulsifier (JDD).The emulsifier tank (JDB) has an interior (JDC), an emulsifier input(JDF), an emulsifier conveyor (JDG), and an emulsifier conveyor output(JDH). The emulsifier tank (JDB) accepts an emulsifier (JDD) to theinterior (JDC) and regulates and controls an engineered amount ofemulsifier (JDD) downstream to be mixed to form an emulsion. Theemulsifier conveyor (6B5) has an integrated mass sensor (JDJ) that isconfigured to input and output a signal (JDK) to the computer (COMP).The emulsifier conveyor motor (JDL) has a controller (JDM) that isconfigured to input and output a signal (JDN) to the computer (COMP).The mass sensor (JDJ), emulsifier conveyor (JDG), and emulsifierconveyor motor (JDL) are coupled so as to permit the conveyance,distribution, or output of a precise flow of emulsifier (JDD) via anemulsifier transfer line (JDI). It is to be noted that the emulsifiermay be in solid, powder, liquid, or slurry form. Transferring anengineered amount of emulsifier (JDD) downstream to be mixed to form anemulsion is the premise of the disclosure and is not limited toregulating as a solid, powder, liquid, gel, slurry, or the equivalent.

FIG. 17J′ displays an extract distribution system (JEA) including anextract tank (JEB) that is configured to accept an extract (JED). Theextract tank (JEB) has an interior (JEC), an extract input (JEF), anextract conveyor (JEG), and an extract conveyor output (JEH). Theextract tank (JEB) accepts an extract (JED) to the interior (JEC) andregulates and controls an engineered amount of extract (JED) downstreamto be mixed to form an emulsion. The extract conveyor (6B5) has anintegrated mass sensor (JEJ) that is configured to input and output asignal (JEK) to the computer (COMP). The extract conveyor motor (JEL)has a controller (JEM) that is configured to input and output a signal(JEN) to the computer (COMP). The mass sensor (JEJ), extract conveyor(JEG), and extract conveyor motor (JEL) are coupled so as to permit theconveyance, distribution, or output of a precise flow of extract (JED)via an extract transfer line (JEI). It is to be noted that the extractmay be in solid, powder, liquid, or slurry form. Transferring anengineered amount of extract (JED) downstream to be mixed to form anemulsion is the premise of the disclosure and is not limited toregulating as a solid, powder, liquid, gel, slurry, or the equivalent.

In embodiments, the extract is not only including from: (VOLT) from FIG.17A′ or 17B′, (SVSM) from FIG. 17C′, (CVOLT) from FIG. 17D′, volatilesfrom FIG. 17E′, and/or extract from FIG. 17H′. In embodiments, theextract comes from any disclosed Figure in this patent specification.

FIG. 17J′ displays an insect distribution system (JFA) including aninsect tank (JFB) that is configured to accept an insect (JFD). Theinsect tank (JFB) has an interior (JFC), an insect input (JFF), aninsect conveyor (JFG), and an insect conveyor output (JFH). The insecttank (JFB) accepts an insect (JFD) to the interior (JFC) and regulatesand controls an engineered amount of insects (JFD) downstream to bemixed to form an emulsion. The insect conveyor (6B5) has an integratedmass sensor (JFJ) that is configured to input and output a signal (JFK)to the computer (COMP). The insect conveyor motor (JFL) has a controller(JFM) that is configured to input and output a signal (JFN) to thecomputer (COMP). The mass sensor (JFJ), insect conveyor (JFG), andinsect conveyor motor (JFL) are coupled so as to permit the conveyance,distribution, or output of a precise flow of insects (JFD) via an insecttransfer line (JFI). It is to be noted that the insects may be in solid,powder, liquid, or slurry form. Transferring an engineered amount ofinsects (JFD) downstream to be mixed to form an emulsion is the premiseof the disclosure and is not limited to regulating as a solid, powder,liquid, gel, slurry, or the equivalent.

FIG. 17J′ displays a biomass distribution system (JGA) including abiomass tank (JGB) that is configured to accept biomass (JGD). Thebiomass tank (JGB) has an interior (JGC), a biomass input (JGF), abiomass conveyor (JGG), and a biomass conveyor output (JGH). The biomasstank (JGB) accepts biomass (JGD) to the interior (JGC) and regulates andcontrols an engineered amount of biomass (JGD) downstream to be mixed toform an emulsion. The biomass conveyor (6B5) has an integrated masssensor (JGJ) that is configured to input and output a signal (JGK) tothe computer (COMP). The biomass conveyor motor (JGL) has a controller(JGM) that is configured to input and output a signal (JGN) to thecomputer (COMP). The mass sensor (JGJ), biomass conveyor (JGG), andbiomass conveyor motor (JGL) are coupled so as to permit the conveyance,distribution, or output of a precise flow of biomass (JGD) via a biomasstransfer line (JGI). It is to be noted that the biomass may be in solid,powder, liquid, or slurry form. Transferring an engineered amount ofbiomass (JGD) downstream to be mixed to form an emulsion is the premiseof the disclosure and is not limited to regulating as a solid, powder,liquid, gel, slurry, or the equivalent.

In embodiments, an emulsion mixing tank (JLE) is configured to acceptacid and/or caustic (JAD) via an acid-caustic transfer line (JAI),biocatalyst (JBD) via a biocatalyst transfer line (JBI), drugs (JCD) viaa drug transfer line (JCI), emulsifier (JDD) via an emulsifier transferline (JDI), extract (JED) via an extract transfer line (JEI), as a firstinput (JLA) through a first input (JLA). In embodiments, an emulsionmixing tank (JLE) is configured to accept insects (JFD) via an insecttransfer line (JFI), and biomass (JGD) via a biomass transfer line (JGI)as a second mixture (JLD) through a second input (JLC). It is to benoted that the first input (JLA) through a first input (JLA) and thesecond mixture (JLD) through a second input (JLC) are non-limiting andit is true that each of the acid and/or caustic (JAD), biocatalyst(JBD), drugs (JCD), emulsifier (JDD), extract (JED), insects (JFD), andbiomass (JGD) through one input or each having their own input to theemulsion mixing tank (JLE). In embodiments, the mixing tank (G15) asshown in FIG. 14G (of Volume I) is the same vessel as the emulsionmixing tank (JLE) as shown in FIG. 17J′ (of Volume II).

In embodiments, a water supply (JKA) is made available to the emulsionmixing tank (JLE). In embodiments, a water supply (JKA) transferred tothe emulsion mixing tank (JLE) is first treated in a first watertreatment unit (JKB), second water treatment unit (JKC), and a thirdwater treatment unit (JKD) to form treated water (JKE).

In embodiments, the first water treatment unit (JKB) includes one ormore selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the second water treatment unit (JKC) includesone or more selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the third water treatment unit (JKD) includesone or more selected from the group consisting of a cation, an anion, amembrane, a filter, activated carbon, an adsorbent, an absorbent, anultraviolet unit, an ozone unit, a microwave unit, and/or a distillationsystem. In embodiments, the adsorbent includes one or more selected fromthe group consisting of 3 Angstrom molecular sieve, 3 Angstrom zeolite,4 Angstrom molecular sieve, 4 Angstrom zeolite, activated alumina,activated carbon, adsorbent, alumina, carbon, catalyst, clay, desiccant,molecular sieve, polymer, resin, and silica gel. In embodiments, thecation is configured to remove positively charged ions from the watersupply (JKA), the positively charged ions are comprised of one or morefrom the group consisting of calcium, magnesium, sodium, and iron. Inembodiments, the anion is configured to remove negatively charged ionsfrom the water supply (JKA), the negatively charged ions are comprisedof one or more from the group consisting of iodine, chloride, andsulfate. In embodiments, the membrane is configured to removeundesirable compounds from the water supply (JKA), the undesirablecompounds are comprised of one or more from the group consisting ofdissolved organic chemicals, viruses, bacteria, and particulates. Inembodiments, the membrane has a diameter that ranges from 1 inch to 6inches and a pore size ranging from 0.0001 microns to 0.5 microns.

In embodiments, the water treatment unit in any embodiment described inVolume I or Volume II) includes a distillation system. In embodiments,treated water is treated with a distillation system. In embodiments, theelectrical conductivity of the treated water treated by the distillationsystem includes one or more selected from the group consisting of: 0.1μS to 0.5 μS, 0.50 μS, to 1.00 μS, 1.000 μS, to 1.25 μS, 1.250 μS, to1.50 μS, 1.500 μS, to 1.75 μS, 1.750 μS, to 2.00 μS, 2.00 μS to 2.25 μS,2.25 μS to 2.50 μS, 2.50 μS to 2.75 μS, 2.75 μS to 3.00 μS, 3.00 μS to3.25 μS, 3.25 μS to 3.50 μS, 3.50 μS to 3.75 μS, 3.75 μS to 4.00 μS,4.00 μS to 4.25 μS, 4.25 μS to 4.50 μS, 4.50 μS to 4.75 μS, 4.75 μS to5.00 μS, 5.00 μS to 5.25 μS, 5.25 μS to 5.50 μS, 5.50 μS to 5.75 μS,5.75 μS to 6.00 μS, 6.00 μS to 6.25 μS, 6.25 μS to 6.50 μS, 6.50 μS to6.75 μS, 6.75 μS to 7.00 μS, 7.00 μS to 7.25 μS, 7.25 μS to 7.50 μS,7.50 μS to 7.75 μS, 7.75 μS to 8.00 μS, 8.00 μS to 8.25 μS, 8.25 μS to8.50 μS, 8.50 μS to 8.75 μS, 8.75 μS to 9.00 μS, 9.00 μS to 9.25 μS,9.25 μS to 9.50 μS, 9.50 μS to 9.75 μS, 9.75 μS to 10.00 μS. Inembodiments, μS means μS per centimeter.

In embodiments, treated water (JKE) is discharged from the first watertreatment unit (JKB), second water treatment unit (JKC), and/or thethird water treatment unit (JKD). In embodiments, treated water (JKE)has less positively charged ions, negatively charged ions, andundesirable compounds relative to the supply (JKA). In embodiments, avalve (HJI) is configured to regulate the flow of the treated water(HJA) that leaves the first water treatment unit (HJK), second watertreatment unit (HJL), and/or the third water treatment unit (HJM). Inembodiments, a quality sensor (JKG) is configured to measure the qualityof the treated water (JKE) that leaves the first water treatment unit(HJK), second water treatment unit (HJL), and/or the third watertreatment unit (HJM). For example, the quality sensor (JKG) may measurethe electrical conductivity of the treated water (JKE) to determine ifeither of the first water treatment unit (HJK), second water treatmentunit (HJL), and/or the third water treatment unit (HJM) requiremaintenance and/or cleaning. In embodiments, the quality sensor (HJN)measures the electrical conductivity of the treatment unit (HJM) toensure that the electrical conductivity ranges from 0.10 microsiemensper centimeter to 100 microsiemens per centimeter.

In embodiments, a treated water pump (JKH) is provided and is configuredto accept the treated water (JKE) from either one of the first watertreatment unit (HJK), second water treatment unit (HJL), and/or thethird water treatment unit (HJM). In embodiments, a valve (JKK) isconfigured to regulate the flow of the treated water (JKE) that leavesthe treated water pump (JKH). In embodiments, a pressure sensor (HFB) isconfigured to measure the pressure of the treated water (JKE) thatleaves the treated water pump (JKH). In embodiments, a flow sensor (HFC)is configured to measure the flow of the treated water (JKE) that leavesthe treated water pump (JKH). In embodiments, the treated water (JKE)that leaves the treated water pump (JKH) has a pressure that includesone or more pressure ranges selected from the group consisting of 10pounds per square inch (PSI) to 20 PSI, 20 PSI to 40 PSI, 40 PSI to 60PSI, 60 PSI to 80 PSI, 80 PSI to 100 PSI, 100 PSI to 125 PSI, 125 PSI to150 PSI, 150 PSI to 175 PSI, 175 PSI to 200 PSI, 200 PSI to 225 PSI, 225PSI to 250 PSI, 250 PSI to 275 PSI, 275 PSI to 300 PSI, 300 PSI to 325PSI, 325 PSI to 350 PSI, 350 PSI to 375 PSI, 375 PSI to 400 PSI, 400 PSIto 425 PSI, 425 PSI to 450 PSI, 450 PSI to 475 PSI, and 475 PSI to 500PSI.

In embodiments, an emulsion mixing tank (JLE) is provided to mix theacid and/or caustic (JAD), biocatalyst (JBD), drugs (JCD), emulsifier(JDD), extract (JED), insects (JFD), and biomass (JGD) through one inputor each having their own input to the emulsion mixing tank (JLE).

In embodiments, an emulsion mixing tank (JLE) has an interior (JLF). Inembodiments, the emulsion mixing tank (JLE) has have a heating jacket(JLN) to serve the purpose of the heat exchanger (JLM). The emulsionmixing tank (JLE) with a heating jacket (JLN) is a vessel that isdesigned for controlling the temperature of its contents, by using aheating jacket around the vessel through which a heat transfer medium(e.g.—steam) is circulated. The heating jacket (JLN) is a cavityexternal to the interior (JLF) of the emulsion mixing tank (JLE) thatpermits the uniform exchange of heat between the heat transfer mediumcirculating in it and the walls of the emulsion mixing tank (JLE). FIG.17J′ shows the heating jacket (JLN) installed over a portion of theemulsion mixing tank (JLE) creating an interior (JLO) having an annularspace within which a heat transfer medium flows.

The heating jacket (JLN) has a heat transfer medium inlet (JLP) and aheat transfer medium outlet (JLQ). Steam (JLR) is introduced to the heattransfer medium inlet (JLP). Steam condensate (JLT) is discharged fromthe heat transfer medium outlet (JLQ). Steam (JLR) is introduced to theheat transfer medium inlet (JLP) of the heating jacket (JLN) of theemulsion mixing tank (JLE) via a steam inlet conduit (JLS). The steaminlet conduit (JLS) is connected to the heat transfer medium inlet (JLP)and is configured to transfer steam (JLR) to the interior (JLO) of theheating jacket (JLN).

In embodiments, a steam supply (LDM′) is provided to the heating jacket(JLN) and/or to the heat exchanger (JLM) and is provided from FIG. 17F′.In embodiments, the steam condensate (JLT) that is discharged from theheat transfer medium outlet (JLQ) is transferred to the condensate tank(LAP) shown in FIG. 17F′.

A steam supply valve (JLU) is interposed on the steam inlet conduit(JLS). The steam supply valve (JLU) is equipped with a controller (JLV)that inputs and outputs a signal (JLW) to the computer (COMP). Inembodiments, the steam supply valve (JLU) is positioned to regulate themass of heat transfer medium that leaves the heating jacket (JLN) viathe discharged from the heat transfer medium outlet (JLQ).

In embodiments, a temperature sensor (JMA) measures the temperature ofthe contents within the interior (JLF) of the emulsion mixing tank(JLE). The temperature sensor (JMA) is configured to output a signal(JMB) to the computer (COMP). A pre-determined setpoint for the emulsionmixing tank (JLE) temperature sensor (JMA) may be inputted to thecomputer (COMP). In response to the pre-determined setpoint, thecomputer (COMP) regulates the modulation of the steam supply valve(JLU). The preferred modulation range of the steam supply valve (JLU)ranges from 33% open to 66% open. In embodiments, the preferredmodulation range of the steam supply valve (JLU) ranges from: 5% open to10% open; 10% open to 15% open; 15% open to 20% open; 20% open to 30%open; 30% open to 40% open; 40% open to 50% open; 50% open to 60% open;60% open to 70% open.

In embodiments, the emulsion mixing tank (JLE) has a plurality ofbaffles (JLI, JLJ) that are positioned within the interior (JLF). Eachbaffle (JLI, JLJ) is configured to promote mixing and increase heattransfer and to create an emulsion.

The pressure drop across the steam supply valve (JLU) ranges frombetween: 1 pound per square inch (PSI) to 2 PSI; 2 pounds per squareinch (PSI) to 5 PSI; 5 pounds per square inch (PSI) to 10 PSI; 10 poundsper square inch (PSI) to 20 PSI; 20 pounds per square inch (PSI) to 40PSI; 40 pounds per square inch (PSI) to 60 PSI; 60 pounds per squareinch (PSI) to 80 PSI; 80 pounds per square inch (PSI) to 100 PSI; 100pounds per square inch (PSI) to 125 PSI; 125 pounds per square inch(PSI) to 150 PSI; 150 pounds per square inch (PSI) to 200 PSI.

The velocity of steam in the steam inlet conduit (JLR) ranges from: 35feet per second to 45 feet per second; 45 feet per second to 55 feet persecond; 55 feet per second to 65 feet per second; 65 feet per second to75 feet per second; 75 feet per second to 85 feet per second; 85 feetper second to 95 feet per second; 95 feet per second to 105 feet persecond; 105 feet per second to 115 feet per second; 115 feet per secondto 125 feet per second; 125 feet per second to 135 feet per second; 135feet per second to 145 feet per second; 145 feet per second to 155 feetper second; 155 feet per second to 175 feet per second. The velocity ofsteam condensate discharged from the heat transfer medium outlet (G91)is less than 3 feet per second.

In embodiments, the heat transfer medium inlet (JLP) is comprised of oneor more from the group consisting of: a Class 150 flange, a Class 300flange, sanitary clamp fitting, national pipe thread, or compressionfitting. In embodiments, the heat transfer medium outlet (JLQ) iscomprised of one or more from the group consisting of: a Class 150flange, a Class 300 flange, sanitary clamp fitting, national pipethread, or compression fitting. In embodiments, the emulsion mixing tank(JLE) is comprised of stainless steel or carbon steel and may be ceramicor glass-lined. In embodiments, the heating jacket (JLN) is comprised ofstainless steel or carbon steel and may be ceramic or glass-lined.

In embodiments, the temperature of the mixture within the interior (JLF)of the emulsion mixing tank (JLE) ranges from between: 50 degrees F. to60 degrees F.; 60 degrees F. to 70 degrees F.; 70 degrees F. to 80degrees F.; 80 degrees F. to 90 degrees F.; 90 degrees F. to 100 degreesF.; 100 degrees F. to 110 degrees F.; 110 degrees F. to 120 degrees F.;120 degrees F. to 130 degrees F.; 130 degrees F. to 140 degrees F.; 140degrees F. to 150 degrees F.; 150 degrees F. to 160 degrees F.; 160degrees F. to 170 degrees F.; 170 degrees F. to 180 degrees F.; 180degrees F. to 190 degrees F.; 190 degrees F. to 200 degrees F.; 200degrees F. to 212 degrees F.

In embodiments, the mixture may mixed within the interior (JLF) of theemulsion mixing tank (JLE) ranges from between: 1 minute to 5 minutes, 5minutes to 10 minutes; 10 minutes to 20 minutes; 20 minutes to 30minutes; 30 minutes to 40 minutes; 40 minutes to 50 minutes; 50 minutesto 1 hour; 1 hour to 1.5 hours; 1.5 hour to 2 hours; 2 hour to 3 hours;3 hour to 4 hours; 4 hour to 5 hours; 5 hour to 6 hours; 6 hour to 12hours; 12 hour to 18 hours; 18 hour to 24 hours; 1 day to 2 days; 2 daysto 3 days; 3 days to 4 days; 4 days to 5 days; 5 days to 1 week.

In embodiments, the emulsion mixing tank (JLE) is equipped with a pHsensor (JMC) that is configured to input a signal (JMD) to the computer(COMP). In embodiments, the emulsion mixing tank (JLE) is equipped witha first emulsifier system (JME). In embodiments, the first emulsifiersystem (JME) is an ultrasonic homogenizer (JME′). In embodiments, theultrasonic homogenizer (JME′) is equipped with a controller (JMF) thatis equipped to send a signal (JMG) to and from the computer (COMP).

In embodiments, the emulsion mixing tank (JLE) has a mixture output(JMH) that discharges a mixture (JMI) from within the interior (JLF) ofthe emulsion mixing tank (JLE). In embodiments, the mixture (JMI) thatis discharged from the interior (JLF) of the emulsion mixing tank (JLE)is an emulsion (JMX). In embodiments, the mixture (JMI) that isdischarged from the interior (JLF) of the emulsion mixing tank (JLE) istransferred to a mixture pump (JMJ). In embodiments, the mixture pump(JMJ) pumps and pressurizes the mixture (JMI) that is discharged fromthe interior (JLF) of the emulsion mixing tank (JLE) to form apressurized mixture (JMK). A pressure sensor (JML) is installed tomeasure the pressure of the pressurized mixture (JMK) and transmit asignal (JMM) to the computer (COMP). In embodiments, the pressurizedmixture (JMK) is transferred to a second emulsifier system (JMN).

In embodiments, the second emulsifier system (JMN) accepts thepressurized mixture (JMK) via a mixture input (JMV). In embodiments, thesecond emulsifier system (JMN) has an emulsion output (JMW) fordischarging an emulsion (JMX). In embodiments, the pressurized mixture(JMK) is a first emulsion (JMY) and the emulsion (JMX) discharged fromthe second emulsifier system (JMN) is the second emulsion (JMZ). Inembodiments, at least a portion of the emulsion (JMX) discharged fromthe second emulsifier system (JMN) is returned to the interior (JLF) ofthe emulsion mixing tank (JLE) via a recycle conduit (JNA) and a recycleinput (JNB). In embodiments, at least a portion of the emulsion (JMX)discharged from the second emulsifier system (JMN) is an emulsionproduct (JNC) or a pressurized emulsion product (JND).

A flow sensor (JNE) is configured to measure the flow rate of theemulsion product (JNC) and input a signal (JNF) to the computer (COMP).An emulsion product valve (JNG) is configured to regulate the flow ofthe emulsion product (JNC) and the emulsion product valve (JNG) isequipped with a controller (JNH) that inputs or outputs a signal (JNI)to the computer (COMP). In embodiments, the second emulsifier system(JMN) has an interior (JMO) and is equipped with a motor (JMP) that hasa controller (JMQ) and is configured to input or output a signal (JMR)to the computer (COMP). In embodiments, the second emulsifier system(JMN) is equipped with a piston (JMS), a rotor-stator (JMT), or a valveand seat (JMU).

The emulsion mixing tank (JLE) may be equipped with a mixer (JLK) formixing the contents of the interior (JLF) of the emulsion mixing tank(JLE). The mixer (JLK) may be of an auger or blade type that is equippedwith a motor (JLL).

In embodiments, when the low-level sensor (JLH) sends a signal to thecomputer (COMP), the valve (JKK) on the discharge of the water pump(JKH) may be opened to introduce water into the interior (JLF) of theemulsion mixing tank (JLE) until the high-level sensor (JLG) istriggered thus sending a signal to the computer (COMP) to close thevalve (JKK). This level control loop including the high-level sensor(JLG) for detecting a high level and a low-level sensor (JLH) fordetecting a lower level may be coupled to the operation of the watersupply valve (JKK) for introducing a treated water (JKE) through a firstwater treatment unit (JKB), a second water treatment unit (JKC), and athird water treatment unit (JKD) and into the interior (JLF) of theemulsion mixing tank (JLE).

In embodiments, the treated water (JKL) is transferred from the waterpump (JKH) to form pressurized treated water (JKL). In embodiments, thepressurized treated water (JKL) is transferred through a water transferconduit (JKM) and through a valve (JKK). In embodiments, as thepressurized treated water (JKL) passes through the valve (JKK) on thewater transfer conduit (JKM), the pressurized treated water (JKL) isreduced in pressure to form a depressurized treated water (JKN) which isthen introduced to the interior (JLF) of the emulsion mixing tank (JLE)via a water input (JKO).

In embodiments, a gas tank (JJA) is provided. In embodiments, the gastank (JJA) contains a gas (JJB). In embodiments, the gas (JJB) istransferred from the gas tank (JJA) and is made available to theinterior (JLF) of the emulsion mixing tank (JLE) as a gas supply (JJC).A pressure sensor (JJD) is installed to measure the pressure of the gas(JJB) within the gas tank (JJA). A pressure regulating valve (JJE) isprovided to set a pressure of the gas supply conduit (JJP) to transfergas (JJB) from the gas tank (JJA) into the interior (JLF) of theemulsion mixing tank (JLE).

A pressure sensor (JJI) is provided to measure the pressure within thegas supply conduit (JJP) and input a signal (JJH) to the computer(COMP). In embodiments, a first gas valve (JJJ) is provided to regulatethe flow of gas (JJB) from the gas supply conduit (JJP) and into theinterior (JLF) of the emulsion mixing tank (JLE). The first gas valve(JJJ) has a controller (JJF) that is equipped to input or output asignal (JJG) to the computer (COMP). In embodiments, a second gas valve(JJK) is provided to regulate the flow of gas (JJB) from the gas supplyconduit (JJP) and into the interior (JLF) of the emulsion mixing tank(JLE). The second gas valve (JJK) has a controller (JJL) that isequipped to input or output a signal (JJM) to the computer (COMP). Apressure sensor (JJO) is provided to measure the pressure within the gassupply conduit (JJP) downstream of both the first gas valve (JJJ) andsecond gas valve (JJK) and input a signal (JJN) to the computer (COMP).A first one-way valve (JJT) is installed on the gas supply conduit (JJP)downstream of both of the first gas valve (JJJ) and second gas valve(JJK) and before the gas input (JJY) of the emulsion mixing tank (JLE).In embodiments, a second one-way valve (JJU) is provided to preventback-flow of recycled carbon dioxide (JJX) from the gas input (JJY) ofthe emulsion mixing tank (JLE) backwards to the CO2 recovery system onFIG. 17G.

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: acidifying agents (acetic acid, glacial acetic acid, citric acid,fumaric acid, hydrochloric acid, diluted hydrochloric acid, malic acid,nitric acid, phosphoric acid, diluted phosphoric acid, sulfuric acid,tartaric acid).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: alkalizing agents (ammonia solution, ammonium carbonate,diethanolamine, diisopropanolamine, potassium hydroxide, sodiumbicarbonate, sodium borate, sodium carbonate, sodium hydroxide,trolamine).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: antifoaming agents (dimethicone, simethicone).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: antimicrobial preservatives (benzalkonium chloride, benzalkoniumchloride solution, benzethonium chloride, benzoic acid, benzyl alcohol,butylparaben, cetylpyridinium chloride, chlorobutanol, chlorocresol,cresol, dehydroacetic acid, ethylparaben, methylparaben, methylparabensodium, phenol, phenylethyl alcohol, phenylmercuric acetate,phenylmercuric nitrate, potassium benzoate, potassium sorbate,propylparaben, propylparaben sodium, sodium benzoate, sodiumdehydroacetate, sodium propionate, sorbic acid, thimerosal, thymol).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: antioxidants (ascorbic acid, ascorbyl palmitate, butylatedhydroxyanisole, butylated hydroxytoluene, hypophosphorous acid,monothioglycerol, propyl gallate, sodium formaldehyde sulfoxylate,sodium metabisulfite, sodium thiosulfate, sulfur dioxide, tocopherol,tocopherols excipient).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: buffering agents (acetic acid, ammonium carbonate, ammoniumphosphate, boric acid, citric acid, lactic acid, phosphoric acid,potassium citrate, potassium metaphosphate, potassium phosphatemonobasic, sodium acetate, sodium citrate, sodium lactate solution,dibasic sodium phosphate, monobasic sodium phosphate).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: chelating agents (edetate disodium, ethylenediaminetetraaceticacid and salts, edetic acid).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: coating agents (sodium carboxymethylcellulose, cellulose acetate,cellulose acetate phthalate, ethylcellulose, gelatin, pharmaceuticalglaze, hydroxypropyl cellulose, hydroxypropyl methylcellulose,hydroxypropyl methylcellulose phthalate, methacrylic acid copolymer,methylcellulose, polyvinyl acetate phthalate, shellac, sucrose, titaniumdioxide, carnauba wax, microcrystalline wax, zein); Colorants (caramel,red, yellow, black or blends, ferric oxide).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: complexing agents (ethylenediaminetetraacetic acid and salts(EDTA), edetic acid, gentisic acid ethanolamide, oxyquinoline sulfate);Desiccants (calcium chloride, calcium sulfate, silicon dioxide).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: emulsifying and/or solubilizing agents (acacia, cholesterol,diethanolamine (adjunct), glyceryl monostearate, lanolin alcohols, mono-and di-glycerides, monoethanolamine (adjunct), lecithin, oleic acid(adjunct), oleyl alcohol (stabilizer), poloxamer, polyoxyethylene 50stearate, polyoxyl 35 castor oil, polyoxyl 40 hydrogenated castor oil,polyoxyl 10 oleyl ether, polyoxyl 20 cetostearyl ether, polyoxyl 40stearate, polysorbate 20, polysorbate 40, polysorbate 60, polysorbate80, diacetate, monostearate, sodium lauryl sulfate, sodium stearate,sorbitan monolaurate, sorbitan monooleate, sorbitan monopalmitate,sorbitan monostearate, stearic acid, trolamine, emulsifying wax).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: filtering aids (powdered cellulose, purified siliceous earth);Flavors and perfumes (anethole, benzaldehyde, ethyl vanillin, menthol,methyl salicylate, monosodium glutamate, orange flower oil, peppermint,peppermint oil, peppermint spirit, rose oil, stronger rose water,thymol, tolu balsam tincture, vanilla, vanilla tincture, vanillin).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: humectants (glycerol, hexylene glycol, sorbitol).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: plasticizers (e.g., castor oil, diacetylated monoglycerides,diethyl phthalate, glycerol, mono- and di-acetylated monoglycerides,propylene glycol, triacetin, triethyl citrate).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: polymers (e.g., cellulose acetate, alkyl celluloses, hydroxyalkyl,acrylic polymers and copolymers).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: solvents (acetone, alcohol, diluted alcohol, amylene hydrate,benzyl benzoate, butyl alcohol, carbon tetrachloride, chloroform, cornoil, cottonseed oil, ethyl acetate, glycerol, hexylene glycol, isopropylalcohol, methyl alcohol, methylene chloride, methyl isobutyl ketone,mineral oil, peanut oil, propylene carbonate, sesame oil, treatedwater).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: sorbents (powdered cellulose, charcoal, purified siliceous earth).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: carbon dioxide sorbents (barium hydroxide lime, soda lime).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: stiffening agents (hydrogenated castor oil, cetostearyl alcohol,cetyl alcohol, cetyl esters wax, hard fat, paraffin, polyethyleneexcipient, stearyl alcohol, emulsifying wax, white wax, yellow wax).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: suspending and/or viscosity-increasing agents (acacia, agar,alginic acid, aluminum monostearate, bentonite, purified bentonite,magma bentonite, carbomer, carboxymethylcellulose calcium,carboxymethylcellulose sodium, carboxymethylcellulose sodium 12,carrageenan, microcrystalline and carboxymethylcellulose sodiumcellulose, dextrin, gelatin, guar gum, hydroxyethyl cellulose,hydroxypropyl cellulose, hydroxypropyl methylcellulose, magnesiumaluminum silicate, methylcellulose, pectin, polyethylene oxide,polyvinyl alcohol, povidone, alginate, silicon dioxide, colloidalsilicon dioxide, sodium alginate, tragacanth, xanthan gum).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: sweetening agents (aspartame, dextrates, dextrose, excipientdextrose, fructose, mannitol, saccharin, calcium saccharin, sodiumsaccharin, sorbitol, solution sorbitol, sucrose, compressible sugar,confectioner's sugar, syrup).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: surfactants (simethicone).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: tablet binders (acacia, alginic acid, sodiumcarboxymethylcellulose, microcrystalline cellulose, dextrin,ethylcellulose, gelatin, liquid glucose, guar gum, hydroxypropylmethylcellulose, methylcellulose, polyethylene oxide, povidone,pregelatinized starch, syrup).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: tablet and/or capsule diluents (calcium carbonate, dibasic calciumphosphate, tribasic calcium phosphate, calcium sulfate, microcrystallinecellulose, powdered cellulose, dextrates, dextrin, dextrose excipient,fructose, kaolin, lactose, mannitol, sorbitol, starch, pregelatinizedstarch, sucrose, compressible sugar, confectioner's sugar).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: tablet disintegrants (alginic acid, microcrystalline cellulose,croscarmellose sodium, crospovidone, polacrilin potassium, sodium starchglycolate, starch, pregelatinized starch).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: tablet and/or capsule lubricants (calcium stearate, glycerylbehenate, magnesium stearate, light mineral oil, sodium stearylfumarate, stearic acid, purified stearic acid, talc, hydrogenatedvegetable oil, zinc stearate).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: thickening agents (gelatin having a Bloom strength of 50-100, ananimal-free gelatin, a vegan gelatin, agar, agar-agar, kanten,carrageenan, carrageen, or irish moss vegan jel (vegetable gum adipicacid, tapioca dextrin, calcium phosphate, and potassium citrate)).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: tonicity agent (dextrose, glycerol, mannitol, potassium chloride,sodium chloride).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: a flavoring and/or sweetener (aromatic elixir, compoundbenzaldehyde elixir, iso-alcoholic elixir, peppermint water, sorbitolsolution, syrup, tolu balsam syrup).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: an oleaginous compound (almond oil, corn oil, cottonseed oil,ethyl oleate, isopropyl myristate, isopropyl palmitate, mineral oil,light mineral oil, myristyl alcohol, octyl dodecanol, olive oil, peanutoil, persic oil, sesame oil, soybean oil, squalane).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: a sterile compound (Bacteriostatic water for injection,bacteriostatic sodium chloride injection)

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: viscosity-increasing agents (suspending agents, agar agar, calciumalginate, curdlan, gelatin, gellan gum, glycerol esters of wood rosin,hydroxypropyl methyl cellulose, jelly powder, konjac gum,microcrystalline cellulose (MCC), pectin, propylene glycol alginate(PGA) semi-refined carrageenan, sodium alginate, sodium carboxymethylcellulose, tamarind gum polysaccharide, tara gum, xanthan gum).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: water repelling agents (cyclomethicone, dimethicone, simethicone).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: a solubilizing agent (benzalkonium chloride, benzethoniumchloride, cetylpyridinium chloride, docusate sodium, nonoxynol 9,nonoxynol 10, octoxynol 9, poloxamer, polyoxyl 35 castor oil, polyoxyl40, hydrogenated castor oil, polyoxyl 50 stearate, polyoxyl 10 oleylether, polyoxyl 20, cetostearyl ether, polyoxyl 40 stearate, polysorbate20, polysorbate 40, polysorbate 60, polysorbate 80, sodium laurylsulfate, sorbitan monolaurate, sorbitan monooleate, sorbitanmonopalmitate, sorbitan monostearate, tyloxapol).

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith: one or more waxes selected from the group consisting of acaciadecurrens flower cera (mimosa flower wax), almond wax, avocado wax,beery wax, bees wax, cananga odorata flower cera (ylang ylang flowerwax), candelilla wax, Cannabis sativa oil, castor wax, cupuacu butter,floral wax, hemp wax, hydrogenated almond oil, hydrogenated animal-basedoils, hydrogenated apricot kernel oil, hydrogenated avocado oil,hydrogenated brazil nut oil, hydrogenated canola oil, hydrogenatedcashew oil, hydrogenated cocoa butter, hydrogenated coconut oil,hydrogenated coffee oil, hydrogenated corn oil, hydrogenated cottonseedoil, hydrogenated grapeseed oil, hydrogenated hazelnut oil, hydrogenatedhemp oil, hydrogenated hop oil, hydrogenated insect oil, hydrogenatedlard oil, hydrogenated lard, hydrogenated macadamia nut oil,hydrogenated mustard oil, hydrogenated olive oil, hydrogenated palmkernel oil, hydrogenated palm oil, hydrogenated peanut oil, hydrogenatedpeppermint oil, hydrogenated rapeseed oil, hydrogenated rice bran oil,hydrogenated rice oil, hydrogenated safflower oil, hydrogenatedsemi-refined sesame oil, hydrogenated semi-refined sunflower oil,hydrogenated sesame oil, hydrogenated soybean oil, hydrogenated walnutoil, jasminum grandiflorum flower cera (jasmine flower wax), Lavandulaangustifolia flower cera (lavender flower wax), mmyrica fruit wax, olivewax, prunus amygdalus dulcis oil, rapeseed wax, rice bran wax, rosadamascene flower cera (rose flower wax), shea butter, soybean wax,sunflower wax, vegan wax, vegetable wax, wax from Mexican shrubEuphorbia antisyphilitica, and wax from the berries of rhus verniciflua.

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith esterified insect lipids.

In embodiments, the cannabinoid and/or cannabinoid emulsion may be mixedwith psilocybin mushrooms and/or the alimentary composition and/or thepsilocybin extract, psilocin extract, baeocystin extract, and/ornorbaeocystin extract.

In embodiments, the cannabis described in any of FIGS. in Volume II canbe replaced with the psilocybin mushrooms and/or the alimentarycomposition to produce the psilocybin extract, psilocin extract,baeocystin extract, and/or norbaeocystin extract. In embodiments, thecannabis described in any of FIGS. in Volume II can be mixed with thepsilocybin mushrooms and/or the alimentary composition to produce thecannabinoid extract (such as THC extract and/or CBD extract) along withpsilocybin extract, psilocin extract, baeocystin extract, and/ornorbaeocystin extract. In embodiments, the cannabis described in any ofFIGS. in Volume II can be mixed with the psilocybin mushrooms and/or thealimentary composition to produce the cannabinoid extract (such as THCoil and/or CBD oil) along with psilocybin extract, psilocin extract,baeocystin extract, and/or norbaeocystin extract. In embodiments, thecannabis described in any of FIGS. in Volume II includes a fungus toproduce the cannabinoid extract (such as THC oil and/or CBD oil).

FIG. 17K′

FIG. 17K′ shows one non-limiting embodiment of a cannabinoid softgelencapsulation system (17K).

FIG. 17K′ displays an extract distribution system (KEA) including anextract tank (KEB) that is configured to accept an extract (KED). Theextract tank (KEB) has an interior (KEC), an extract input (KEF), anextract conveyor (KEG), and an extract conveyor output (KEH). Theextract tank (KEB) accepts an extract (KED) to the interior (KEC) andregulates and controls an engineered amount of extract (KED) downstreamto be mixed to form an emulsion. The extract conveyor (KB5) has anintegrated mass sensor (KEJ) that is configured to input and output asignal (KEK) to the computer (COMP). The extract conveyor motor (KEL)has a controller (KEM) that is configured to input and output a signal(KEN) to the computer (COMP). The mass sensor (KEJ), extract conveyor(KEG), and extract conveyor motor (KEL) are coupled so as to permit theconveyance, distribution, or output of a precise flow of extract (KED)via an extract transfer line (KEI) into the input (KDF) of thecannabinoid softgel encapsulation system (17K). It is to be noted thatthe extract may be in solid, powder, crystal, liquid, or slurry form.Transferring an engineered amount of extract (KED) downstream to bemixed to form a softgel (KCC) is the premise of the disclosure and isnot limited at all whatsoever.

The cannabinoid softgel encapsulation system (JKB) shown in FIG. 17K′ isconfigured to produce cannabinoid softgels (KCC). In embodiments, asoftgel (KCC) is an oral dosage form for medicine similar to capsules.In embodiments, softgels (KCC) are comprised of a gelatin based shellsurrounding a liquid fill. In embodiments, the liquid fill is either anemulsion, volatiles from cannabis or DANLEO Jr, or any number ofcombinations and permutations of THC and/or CBD as disclosed in thispatent specification.

In embodiments, softgel shells are a combination of cannabinoids,gelatin, water, and a plasticiser such as glycerin or sorbitol. Inembodiments, the plasticiser is used to increase the plasticity ordecrease the viscosity of a material for the encapsulation ofcannabinoids. In embodiments, the plasticiser is an emulsifier. Inembodiments, softgel shells are a combination of cannabinoids, anemulsifier, medium chain triglycerides, beta caryophyllene, and agelatin shell that includes bovine-derived gelatin, a vegan gelatin,glycerin, sorbitol, and deionized water and/or treated water. Inembodiments, medium chain triglycerides are triglycerides whose fattyacids have an aliphatic tail of 6-12 carbon atoms. In embodiments,triglycerides include esters derived from glycerol and three fatty acids(from tri- and glyceride). In embodiments, the gelatin shell thatincludes gelatin having a Bloom strength of 50-100, an animal-freegelatin, a vegan gelatin, agar, agar-agar, kanten, carrageenan,carrageen, or irish moss vegan jel (vegetable gum adipic acid, tapiocadextrin, calcium phosphate, and potassium citrate). In embodiments, eachsoftgel contains cannabinoids at a cannabinoid concentration rangingfrom one or more cannabinoid concentrations selected from the groupconsisting of 5 mg to 10 mg, 10 mg to 15 mg, 15 mg to 20 mg, 20 mg to 25mg, 25 mg to 30 mg, 30 mg to 35 mg, 35 mg to 40 mg, 40 mg to 45 mg, 45mg to 50 mg, 50 mg to 55 mg, 55 mg to 60 mg, 60 mg to 65 mg, 65 mg to 70mg, 70 mg to 75 mg, 75 mg to 80 mg, 80 mg to 85 mg, 85 mg to 90 mg, 90mg to 95 mg, 95 mg to 100 mg, 100 mg to 125 mg, 125 mg to 150 mg, 150 mgto 175 mg, 175 mg to 200 mg, 200 mg to 225 mg, 225 mg to 250 mg, 250 mgto 275 mg, 275 mg to 300 mg, 300 mg to 325 mg, 325 mg to 350 mg, 350 mgto 375 mg, 375 mg to 400 mg, 400 mg to 425 mg, 425 mg to 450 mg, 450 mgto 475 mg, 475 mg to 500 mg, 500 mg to 550 mg, 550 mg to 600 mg, 600 mgto 650 mg, 650 mg to 700 mg, 700 mg to 750 mg, 750 mg to 800 mg, 800 mgto 850 mg, 850 mg to 900 mg, 900 mg to 950 mg, 950 mg to 1,000 mg, 1,000mg to 2,000 mg, 2,000 mg to 3,000 mg, 3,000 mg to 4,000 mg, 4,000 mg to5,000 mg, 5,000 mg to 6,000 mg, 6,000 mg to 7,000 mg, 7,000 mg to 8,000mg, 8,000 mg to 9,000 mg, and 9,000 mg to 10,000 mg.

In embodiments, the cannabinoid softgel encapsulation system (JKB)includes a rotary die encapsulation system (KAA). In embodiments, rotarydie encapsulation system (KAA) includes a gelatin tank (KBA) having aninterior (KBB). In embodiments, gelatin (KBC) is contained within theinterior (KBB) of the gelatin tank (KBA). In embodiments, gelatin (KBC)is discharged from the gelatin tank (KBA) and is passed through a valve(KBD). A gas supply may pressurize the gelatin tank (KBA), the gassupply system of FIG. 17J′ can be used as similar to the way that thegas supply is provided to the emulsion process. The valve (KBD) has acontroller (KBE) and is configured to input and output a signal (KBF) tothe computer (COMP). A flow sensor (KBG) is provided to measure theamount of gelatin (KBC) transferred from the gelatin tank (KBA) and intothe rotary die encapsulation system (KAA).

In embodiments, the rotary die encapsulation system (KAA) includes aroller (KBH), conveyor (KBI), and a ribbon (KBJ) of gelatin (KBC)(provided from the gelatin tank (KBA)), and a first roller (KCA) and asecond roller (KCB). A softgel (KCC) is created by passing the liquidmixture from within the mixture tank (KDD) through the first roller(KCA) and a second roller (KCB) where the liquid mixture is encapsulatedby the ribbon (KBJ) of gelatin (KBC).

In embodiments, the mixture tank (KDD) contains a variety of cannabinoidproducts from a variety of places and figures discussed in this patentspecification. The mixture tank (KDD) is configured to accept at least:volatiles (VOLT) from FIG. 17A′ or 17B′, a volatiles and solvent mixture(SVSM) from FIG. 17C′, concentrated volatiles (CVOLT) from FIG. 17D′that have undergone evaporation, volatiles from FIG. 17E′, and/orextract from a variety of sources on FIG. 17H′, and the emulsion fromFIG. 17J′, and any combination thereof, or any cannabis extract that isdisclosed in the bounds of this disclosure. In embodiments, the extractcomes from any disclosed figure or text from within this patentspecification.

In embodiments, each softgel has a length and a width. In embodiments,the length of each softgel falls within a range of length that isselected from one or more length ranges consisting from the groupincluding 0.125 inches to 0.250 inches, 0.250 inches to 0.375 inches,0.375 inches to 0.500 inches, 0.500 inches to 0.625 inches, 0.625 inchesto 0.750 inches, 0.750 inches to 0.875 inches, and 0.875 inches to 1.000inch. In embodiments, the width of each softgel falls within a range oflength that is selected from one or more width ranges consisting fromthe group including 0.125 inches to 0.250 inches, 0.250 inches to 0.375inches, 0.375 inches to 0.500 inches, 0.500 inches to 0.625 inches,0.625 inches to 0.750 inches, 0.750 inches to 0.875 inches, and 0.875inches to 1.000 inch. In embodiments, the length is about 0.5 inches andthe width is about 0.313 inches.

In embodiments, each softgel has a mass. In embodiments, the mass ofeach softgel falls within a range of mass that is selected from one ormore mass ranges consisting from the group including 0.500 grams to0.550 grams, 0.550 grams to 0.600 grams, 0.600 grams to 0.650 grams,0.650 grams to 0.700 grams, 0.700 grams to 0.750 grams, 0.750 grams to0.800 grams, 0.800 grams to 0.850 grams, 0.850 grams to 0.900 grams,0.900 grams to 0.950 grams, and 0.950 grams to 1.000 grams.

In embodiments, the thickness of the ribbon (KBJ) of gelatin (KBC) inthe rotary die encapsulation system (KAA) includes one or more selectedfrom the group of ribbon thickness ranges consisting of 0.0050 inches to0.0053 inches, 0.0053 inches to 0.0055 inches, 0.0055 inches to 0.0058inches, 0.0058 inches to 0.0061 inches, 0.0061 inches to 0.0064 inches,0.0064 inches to 0.0067 inches, 0.0067 inches to 0.0070 inches, 0.0070inches to 0.0074 inches, 0.0074 inches to 0.0078 inches, 0.0078 inchesto 0.0081 inches, 0.0081 inches to 0.0086 inches, 0.0086 inches to0.0090 inches, 0.0090 inches to 0.0094 inches, 0.0094 inches to 0.0099inches, 0.0099 inches to 0.0104 inches, 0.0104 inches to 0.0109 inches,0.0109 inches to 0.0115 inches, 0.0115 inches to 0.0120 inches, 0.0120inches to 0.0126 inches, 0.0126 inches to 0.0133 inches, 0.0133 inchesto 0.0139 inches, 0.0139 inches to 0.0146 inches, 0.0146 inches to0.0154 inches, 0.0154 inches to 0.0161 inches, 0.0161 inches to 0.0169inches, 0.0169 inches to 0.0178 inches, 0.0178 inches to 0.0187 inches,0.0187 inches to 0.0196 inches, 0.0196 inches to 0.0206 inches, 0.0206inches to 0.0216 inches, 0.0216 inches to 0.0227 inches, 0.0227 inchesto 0.0238 inches, 0.0238 inches to 0.0250 inches, 0.0250 inches to0.0263 inches, 0.0263 inches to 0.0276 inches, 0.0276 inches to 0.0290inches, 0.0290 inches to 0.0304 inches, 0.0304 inches to 0.0319 inches,0.0319 inches to 0.0335 inches, 0.0335 inches to 0.0352 inches, 0.0352inches to 0.0370 inches, 0.0370 inches to 0.0388 inches, 0.0388 inchesto 0.0407 inches, 0.0407 inches to 0.0428 inches, 0.0428 inches to0.0449 inches, 0.0449 inches to 0.0472 inches, 0.0472 inches to 0.0495inches, 0.0495 inches to 0.0520 inches, 0.0520 inches to 0.0546 inches,0.0546 inches to 0.0573 inches, 0.0573 inches to 0.0602 inches, 0.0602inches to 0.0632 inches, and 0.0632 inches to 0.0664 inches.

In embodiments, the cannabinoid softgel encapsulation system (JKB)includes a washing system (KFA) and a drying system (FGA) that areconfigured to first wash the softgels (KCC) with a wash liquid (KEF) andthen dry the washed softgels (KEJ) in a dryer (KEH) to produce washedand dried softgels (KEK). In embodiments, the wash liquid (KEF) includestreated water (see water treatment system on FIG. 17H′). In embodiments,the wash liquid (KEF) includes an alcohol or a liquid. In embodiments,the wash liquid (KEF) includes ethanol. In embodiments, the washingsystem (KFA) includes a conveyor (KEA) that is configured to accept thesoftgels (KCC) from the first roller (KCA) and a second roller (KCB).

In embodiments, the first roller (KCA) and a second roller (KCB) rotateto form the softgels (KEJ) at a revolutions per minute (RPM) that isselected from one or more from RPMs from the group consisting of 2 rpmto 4 rpm, 4 rpm to 6 rpm, 6 rpm to 8 rpm, 8 rpm to 10 rpm, 10 rpm to 12rpm, 12 rpm to 14 rpm, 14 rpm to 16 rpm, 16 rpm to 18 rpm, 18 rpm to 20rpm, 20 rpm to 22 rpm, 22 rpm to 24 rpm, 24 rpm to 26 rpm, 26 rpm to 28rpm, 28 rpm to 30 rpm, 30 rpm to 32 rpm, 32 rpm to 34 rpm, 34 rpm to 36rpm, 36 rpm to 38 rpm, 38 rpm to 40 rpm, 40 rpm to 42 rpm, 42 rpm to 44rpm, 44 rpm to 46 rpm, 46 rpm to 48 rpm, 48 rpm to 50 rpm, 50 rpm to 52rpm, 52 rpm to 54 rpm, 54 rpm to 56 rpm, 56 rpm to 58 rpm, 58 rpm to 60rpm, 60 rpm to 62 rpm, 62 rpm to 64 rpm, 64 rpm to 66 rpm, 66 rpm to 68rpm, 68 rpm to 70 rpm, and 70 rpm to 85 rpm.

The conveyor (KEA) is equipped with a motor (KEB) and a controller(KEC). The controller (KEC) sends a signal (KED) to and/or from thecomputer (COMP). In embodiments, the conveyor (KEA) is configured toconvey the softgels (KCC) past a washing system (KFA). In embodiments,the washing system (KFA) is configured to wash the softgels (KCC) with awash liquid (KEF) that is dispensed onto the softgels (KCC) through aspray nozzle (KEE) or a plurality of spray nozzles (KEE) to producewashed softgels (KEJ). In embodiments, the pressure drop across thespray nozzle (KEE) or a plurality of spray nozzles (KEE) includes one ormore pressure drop ranges selected from the group consisting of 5 poundsper square inch (PSI) to 10 PSI, 10 PSI to 20 PSI, 20 PSI to 30 PSI, 30PSI to 40 PSI, 40 PSI to 50 PSI, 50 PSI to 60 PSI, 60 PSI to 70 PSI, 70PSI to 80 PSI, 80 PSI to 90 PSI, 90 PSI to 100 PSI, 100 PSI to 125 PSI,125 PSI to 150 PSI, 150 PSI to 175 PSI, 175 PSI to 200 PSI, 200 PSI to225 PSI, 225 PSI to 250 PSI, 250 PSI to 275 PSI, 275 PSI to 300 PSI, 300PSI to 400 PSI, 400 PSI to 500 PSI, 500 PSI to 600 PSI, 600 PSI to 700PSI, 700 PSI to 800 PSI, 800 PSI to 900 PSI, and 900 PSI to 1,000 PSI.

In embodiments, the washed softgels (KEJ) are conveyed away from thewashing system (KFA) and are introduced to the input (KEG) of a dryingsystem (FGA). In embodiments, the drying system (FGA) includes a dryer(KEH) that is configured to dry the washed softgels (KEJ) to producewashed and dried softgels (KEK). In embodiments, the dryer (KEH) is arotary dryer (KEI) that rotates to dry the washed softgels (KEJ) andproduce washed and dried softgels (KEK). In embodiments, the rotarydryer (KEI) rotates to dry the washed softgels (KEJ) and produce washedand dried softgels (KEK) at a revolutions per minute (RPM) that isselected from one or more from RPMs from the group consisting of 2 rpmto 4 rpm, 4 rpm to 6 rpm, 6 rpm to 8 rpm, 8 rpm to 10 rpm, 10 rpm to 12rpm, 12 rpm to 14 rpm, 14 rpm to 16 rpm, 16 rpm to 18 rpm, 18 rpm to 20rpm, 20 rpm to 22 rpm, 22 rpm to 24 rpm, 24 rpm to 26 rpm, 26 rpm to 28rpm, 28 rpm to 30 rpm, 30 rpm to 32 rpm, 32 rpm to 34 rpm, 34 rpm to 36rpm, 36 rpm to 38 rpm, 38 rpm to 40 rpm, 40 rpm to 42 rpm, 42 rpm to 44rpm, 44 rpm to 46 rpm, 46 rpm to 48 rpm, 48 rpm to 50 rpm, 50 rpm to 52rpm, 52 rpm to 54 rpm, 54 rpm to 56 rpm, 56 rpm to 58 rpm, 58 rpm to 60rpm, 60 rpm to 62 rpm, 62 rpm to 64 rpm, 64 rpm to 66 rpm, 66 rpm to 68rpm, 68 rpm to 70 rpm, and 70 rpm to 85 rpm.

In embodiments, the cannabinoid softgel encapsulation system (17K)produces softgels (KCC) that may be in bulk or bottled form. Inembodiments, the cannabinoid softgel encapsulation system (17K) produceswashed and dried softgels (KEK) that may be in bulk or bottled form. Inembodiments, the softgels (KCC, KEK) have a bulk density that includesone or more bulk density ranges selected from the group consisting of 8pounds per cubic foot to 10 pounds per cubic foot, 10 pounds per cubicfoot to 12 pounds per cubic foot, 12 pounds per cubic foot to 14 poundsper cubic foot, 14 pounds per cubic foot to 16 pounds per cubic foot, 16pounds per cubic foot to 18 pounds per cubic foot, 18 pounds per cubicfoot to 20 pounds per cubic foot, 20 pounds per cubic foot to 22 poundsper cubic foot, 22 pounds per cubic foot to 24 pounds per cubic foot, 24pounds per cubic foot to 26 pounds per cubic foot, 26 pounds per cubicfoot to 28 pounds per cubic foot, 28 pounds per cubic foot to 30 poundsper cubic foot, 30 pounds per cubic foot to 32 pounds per cubic foot, 32pounds per cubic foot to 34 pounds per cubic foot, 34 pounds per cubicfoot to 36 pounds per cubic foot, 36 pounds per cubic foot to 38 poundsper cubic foot, 38 pounds per cubic foot to 40 pounds per cubic foot, 40pounds per cubic foot to 42 pounds per cubic foot, 42 pounds per cubicfoot to 44 pounds per cubic foot, 44 pounds per cubic foot to 46 poundsper cubic foot, 46 pounds per cubic foot to 48 pounds per cubic foot, 48pounds per cubic foot to 50 pounds per cubic foot, 50 pounds per cubicfoot to 52 pounds per cubic foot, 52 pounds per cubic foot to 54 poundsper cubic foot, 54 pounds per cubic foot to 56 pounds per cubic foot, 56pounds per cubic foot to 58 pounds per cubic foot, 58 pounds per cubicfoot to 60 pounds per cubic foot, 60 pounds per cubic foot to 62 poundsper cubic foot, 62 pounds per cubic foot to 64 pounds per cubic foot, 64pounds per cubic foot to 66 pounds per cubic foot, 66 pounds per cubicfoot to 68 pounds per cubic foot, 68 pounds per cubic foot to 70 poundsper cubic foot, 70 pounds per cubic foot to 72 pounds per cubic foot, 72pounds per cubic foot to 74 pounds per cubic foot, 74 pounds per cubicfoot to 76 pounds per cubic foot, 76 pounds per cubic foot to 78 poundsper cubic foot, and 78 pounds per cubic foot to 80 pounds per cubicfoot.

FIG. 18′

FIG. 18′ shows a simplistic diagram illustrating a multifunctionalcomposition mixing module (6000) that is configured to generate amultifunctional composition from at least a portion of the cannabis(107, 207) that was harvested from each growing assembly (100, 200). Inembodiments, the cannabis is first trimmed before being mixed with oneor more from the group consisting of fiber-starch, binding agent,density improving textural supplement, moisture improving texturalsupplement, and insects. In embodiments, the cannabis is first trimmedand then grinded before being mixed with one or more from the groupconsisting of fiber-starch, binding agent, density improving texturalsupplement, moisture improving textural supplement, and insects.

FIG. 17′ displays a cannabis distribution module (6A) including acannabis tank (6A2) that is configured to accept at least a portion ofthe cannabis (107, 207) that was harvested from each growing assembly(100, 200). In embodiments, the cannabis is first trimmed before beingintroduced to the cannabis tank (6A). In embodiments, the cannabis isfirst trimmed and then grinded before being introduced to the cannabistank (6A).

The cannabis tank (6A2) has an interior (6A3), a cannabis input (6A4), acannabis conveyor (6A5), and a cannabis conveyor output (6A6). Thecannabis tank (6A2) accepts cannabis to the interior (6A3) and regulatesand controls an engineered amount of cannabis (6A1) downstream to bemixed to form a multifunctional composition. In embodiments, thecannabis tank (6A2) accepts trimmed cannabis (TR1) to the interior(6A3). In embodiments, the cannabis tank (6A2) accepts ground cannabis(GR1) to the interior (6A3).

The cannabis conveyor (6A5) has an integrated cannabis mass sensor (6A7)that is configured to input and output a signal (6A8) to the computer(COMP). The cannabis conveyor motor (6A9) has a controller (6A10) thatis configured to input and output a signal (6A11) to the computer(COMP). The cannabis mass sensor (6A7), cannabis conveyor (6A5), andcannabis conveyor motor (6A9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of cannabis via acannabis transfer line (6A12).

FIG. 17′ displays a fiber-starch distribution module (6B) including afiber-starch tank (6B2) that is configured to accept fiber-starch (6B1).The fiber-starch tank (6B2) has an interior (6B3), a fiber-starch input(6B4), a fiber-starch conveyor (6B5), and a fiber-starch conveyor output(6B6). The fiber-starch tank (6B2) accepts fiber-starch (6B1) to theinterior (6B3) and regulates and controls an engineered amount offiber-starch (6B1) downstream to be mixed to form a multifunctionalcomposition. The fiber-starch conveyor (6B5) has an integratedfiber-starch mass sensor (6B7) that is configured to input and output asignal (6B8) to the computer (COMP). The fiber-starch conveyor motor(6B9) has a controller (6B10) that is configured to input and output asignal (6B11) to the computer (COMP). The fiber-starch mass sensor(6B7), fiber-starch conveyor (6B5), and fiber-starch conveyor motor(6B9) are coupled so as to permit the conveyance, distribution, oroutput of a precise flow of fiber-starch (6B1) via a fiber-starchtransfer line (6B12).

FIG. 17′ displays a binding agent distribution module (6C) including abinding agent tank (6C2) that is configured to accept a binding agent(6C1). The binding agent tank (6C2) has an interior (6C3), a bindingagent input (6C4), a binding agent conveyor (6C5), and a binding agentconveyor output (6C6). The binding agent tank (6C2) accepts bindingagent (6C1) to the interior (6C3) and regulates and controls anengineered amount of a binding agent (6C1) downstream to be mixed toform a multifunctional composition. The binding agent conveyor (6C5) hasan integrated binding agent mass sensor (6C7) that is configured toinput and output a signal (6C8) to the computer (COMP). The bindingagent conveyor motor (6C9) has a controller (6C10) that is configured toinput and output a signal (6C11) to the computer (COMP). The bindingagent mass sensor (6C7), binding agent conveyor (6C5), and binding agentconveyor motor (6C9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of binding agent (6C1) via abinding agent transfer line (6C12).

FIG. 17′ displays a density improving textural supplement distributionmodule (6D) including a density improving textural supplement tank (6D2)that is configured to accept a density improving textural supplement(6D1). The density improving textural supplement tank (6D2) has aninterior (6D3), a density improving textural supplement input (6D4), adensity improving textural supplement conveyor (6D5), and a densityimproving textural supplement conveyor output (6D6). The densityimproving textural supplement tank (6D2) accepts density improvingtextural supplement (6D1) to the interior (6D3) and regulates andcontrols an engineered amount of a density improving textural supplement(6D1) downstream to be mixed to form a multifunctional composition. Thedensity improving textural supplement conveyor (6D5) has an integrateddensity improving textural supplement mass sensor (6D7) that isconfigured to input and output a signal (6D8) to the computer (COMP).The density improving textural supplement conveyor motor (6D9) has acontroller (6D10) that is configured to input and output a signal (6D11)to the computer (COMP). The density improving textural supplement masssensor (6D7), density improving textural supplement conveyor (6D5), anddensity improving textural supplement conveyor motor (6D9) are coupledso as to permit the conveyance, distribution, or output of a preciseflow of density improving textural supplement (6D1) via a densityimproving textural supplement transfer line (6D12).

FIG. 17′ displays a moisture improving textural supplement distributionmodule (6E) including a moisture improving textural supplement tank(6E2) that is configured to accept a moisture improving texturalsupplement (6E1). The moisture improving textural supplement tank (6E2)has an interior (6E3), a moisture improving textural supplement input(6E4), a moisture improving textural supplement conveyor (6E5), and amoisture improving textural supplement conveyor output (6E6). Themoisture improving textural supplement tank (6E2) accepts a moistureimproving textural supplement (6E1) to the interior (6E3) and regulatesand controls an engineered amount of a moisture improving texturalsupplement (6E1) downstream to be mixed to form a multifunctionalcomposition. The moisture improving textural supplement conveyor (6E5)has an integrated moisture improving textural supplement mass sensor(6E7) that is configured to input and output a signal (6E8) to thecomputer (COMP). The moisture improving textural supplement conveyormotor (6E9) has a controller (6E10) that is configured to input andoutput a signal (6E11) to the computer (COMP). The moisture improvingtextural supplement mass sensor (6E7), moisture improving texturalsupplement conveyor (6E5), and moisture improving textural supplementconveyor motor (6E9) are coupled so as to permit the conveyance,distribution, or output of a precise flow of moisture improving texturalsupplement (6E1) via a moisture improving textural supplement transferline (6E12).

FIG. 17′ displays an insect distribution module (6G) including an insecttank (6G2) that is configured to accept insects (6G1). The insect tank(6G2) has an interior (6G3), an insect input (6G4), an insect conveyor(6G5), and an insect conveyor output (6G6). The insect tank (6G2)accepts insects (6G1) to the interior (6G3) and regulates and controlsan engineered amount of insects (6G1) downstream to be mixed to form amultifunctional composition. The insect conveyor (6G5) has an integratedinsect mass sensor (6G7) that is configured to input and output a signal(6G8) to the computer (COMP). The insect conveyor motor (6G9) has acontroller (6G10) that is configured to input and output a signal (6G11)to the computer (COMP). The insect mass sensor (6G7), insect conveyor(6G5), and insect conveyor motor (6G9) are coupled so as to permit theconveyance, distribution, or output of a precise flow of insects (6G1)via an insect transfer line (6G12). In embodiments, the insects may beOrthoptera order of insects including grasshoppers, crickets, cavecrickets, Jerusalem crickets, katydids, weta, lubber, acrida, andlocusts. However, other orders of insects, such as cicadas, ants,mealworms, agave worms, worms, bees, centipedes, cockroaches,dragonflies, beetles, scorpions, tarantulas, termites, insect lipids,and insect oil, or any insects or insect products mentioned herein maybe used as well.

FIG. 17′ displays a multifunctional composition mixing module (6F)including a multifunctional composition tank (6F1) that is configured toaccept a mixture including cannabis, fiber-starch (6B1), binding agent(6C1), density improving textural supplement (6D1), moisture improvingtextural supplement (6E1), and insects (6G1) via a multifunctionalcomposition transfer line (6F0).

The multifunctional composition tank (6F1) has an interior (6F2), amultifunctional composition tank input (6F3), screw conveyor (6F9),multifunctional composition output (6F10). The multifunctionalcomposition tank (6F1) accepts cannabis, fiber-starch (6B1), bindingagent (6C1), density improving textural supplement (6D1), moistureimproving textural supplement (6E1), and insects (6G1) to the interior(6F2) and mixes, regulates, and outputs a weighed multifunctionalcomposition stream (6F22).

The multifunctional composition tank (6F1) has a top section (6F4),bottom section (6F5), at least one side wall (6F6), with a level sensor(6F7) positioned thereon that is configured to input and output a signal(6F8) to the computer (COMP). The screw conveyor (6F9) has amultifunctional composition conveyor motor (6F11) with a controller(6F12) that is configured to input and output a signal (6F13) to thecomputer (COMP). From the multifunctional composition output (6F10) ofthe multifunctional composition tank (6F1) is positioned amultifunctional composition weigh screw (6F14) that is equipped with amultifunctional composition weigh screw input (6F15), a multifunctionalcomposition weigh screw output (6F16), and a mass sensor (6F17) that isconfigured to input and output a signal (6F18) to the computer (COMP).The multifunctional composition weigh screw (6F14) also has a weighscrew motor (6F19) with a controller (6F20) that is configured to inputand output a signal (6F21) to the computer (COMP).

The multifunctional composition mixing module (6000) involves mixing thecannabis with fiber-starch materials, binding agents, density improvingtextural supplements, moisture improving textural supplements, andoptionally insects, to form a multifunctional composition.

The multifunctional composition may be further processed to createfoodstuffs not only including ada, bagels, baked goods, biscuits,bitterballen, bonda, breads, cakes, candies, cereals, chips, chocolatebars, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crêpes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, poffertjes, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,specialty milk, tele-bhaja, tempura, toffee, tortillas, totopo, turkishdelights, or waffles.

In embodiments, the fiber-starch materials may be comprised of singularor mixtures of cereal-grain-based materials, grass-based materials,nut-based materials, powdered fruit materials, root-based materials,tuber-based materials, or vegetable-based materials. In embodiments, thefiber-starch mass ratio ranges from between about 33 pounds offiber-starch per ton of multifunctional composition to about 600 poundsof fiber-starch per ton of multifunctional composition.

In embodiments, the binding agents may be comprised of singular ormixtures of agar, agave, alginin, arrowroot, carrageenan, collagen,cornstarch, egg whites, finely ground seeds, furcellaran, gelatin, guargum, honey, katakuri starch, locust bean gum, pectin, potato starch,proteins, psyllium husks, sago, sugars, syrups, tapioca, vegetable gums,or xanthan gum. In embodiments, the binding agent mass ratio ranges frombetween about 5 pounds of binding agent per ton of multifunctionalcomposition to about 300 pounds of binding agent per ton ofmultifunctional composition.

In embodiments, the density improving textural supplements may becomprised of singular or mixtures of extracted arrowroot starch,extracted corn starch, extracted lentil starch, extracted potato starch,or extracted tapioca starch. In embodiments, the density improvingtextural supplement mass ratio ranges from between about 5 pounds ofdensity improving textural supplement per ton of multifunctionalcomposition to about 300 pounds of density improving textural supplementper ton of multifunctional composition.

In embodiments, the moisture improving textural supplements may becomprised of singular or mixtures of almonds, brazil nuts, cacao,cashews, chestnuts, coconut, filberts, hazelnuts, Indian nuts, macadamianuts, nut butters, nut oils, nut powders, peanuts, pecans, pili nuts,pine nuts, pinon nuts, pistachios, soy nuts, sunflower seeds, tigernuts, and walnuts. In embodiments, the moisture improving texturalsupplement mass ratio ranges from between about 10 pounds of moistureimproving textural supplement per ton of multifunctional composition toabout 1000 pounds of moisture improving textural supplement per ton ofmultifunctional composition.

In embodiments, insects may be added to the multifunctional composition.In embodiments, the insect mass ratio ranges from between about 250pounds of insects per ton of multifunctional composition to about 1500pounds of insects per ton of multifunctional composition.

In embodiments, the cannabis ratio ranges from between about 25 poundsof cannabis per ton of multifunctional composition to about 1800 poundsof cannabis per ton of multifunctional composition. In embodiments, thecannabis ratio ranges from between about 1800 pounds of cannabis per tonof multifunctional composition to about 2000 pounds of cannabis per tonof multifunctional composition. In embodiments, the multifunctionalcomposition includes cannabis, N-acetylglucosamine, bacteria, fungus,and parasites.

The multifunctional composition may solid or liquid and may be includepet foods by further mixing with animal fat, animal protein, animalskin, antibiotics, beef by-product meal, beef meal, beef, carcasses ofbeef, carcasses of chicken, carcasses of fish, carcasses of lamb,carcasses of pigs, chicken by-product meal, chicken meal, chicken,chicken eggs, eggs, fish meal, fish oil, fish scales, flaxseed, lambby-product meal, lamb meal, lamb, mammal by-product meal, mammal meal,pork by-product meal, pork meal, pork, shrimp, soybean oil, or sugar.The compositions disclosed herein may include foods includingcannabinoids including CBD or THC to alleviate arthritis and anxiety inanimals or humans. Compositions disclosed herein may include pet andanimal foods including cannabinoids including CBD or THC to alleviatearthritis and anxiety. Compositions disclosed herein may include pet andanimal foods derived from psilocybin mushrooms or drugs or additives.

In embodiments, the pet food or animal food is fed to pets or animals,the pets or animals include dogs and cats. In embodiments, the pet foodof animal food is fed to pets or animals, the pets or animals includeamphibians, arachnids, arthropods, hexapods, aviary birds, bats, burros,canaries, cats, centipedes, chickens, chinchillas, cockatiels, crabs,crickets, dogs, doves, ducks, falcons, ferrets, finches, freshwaterfish, geese, gerbils, goats, guinea pigs, hamsters, hawks, hedgehogs,horses, invertebrates, insects, land invertebrates, lizards, llamas,lorikeets, lovebirds, mice, miniature horses, mites, worms, mynah birds,octopus, parakeets, parrots, pheasants, pigeons, pond fish, ponies,pot-bellied pigs, quail, rabbits, raccoons, rats, ring-tail possum,saltwater fish, scorpions, short-tailed possum, shrimp, snails,squirrels, sugar gliders, tarantulas, tortoises, toucans, turkeys, orturtles.

In embodiments, the pet food or animal food is fed to pets or animals,the pets or animals include Anthocoridae, minute pirate bugs, piratebugs, flower bugs, the genus Orius, omnivorous bugs, carnivorous bugs,Orthoptera order of insects, grasshoppers, crickets, katydids, weta,lubber, acrida, locusts, mites, spider mites, predatory mites,Neoseiulus Fallacis, genus of mites that are in the Phytoseiidae family,arthropods, hexapods, beetles, cicadas, beetles, nematodes, mealworms,bats, mammals of the order Chiroptera, yellow mealworm beetles, TenebrioMolitor, Tetranychus Urticae, carnivorous arthropods, omnivorousarthropods, green lacewings, insects in the family Chrysopidae, insectsin the order Neuroptera, mantidflies, black soldier flies, black soldierfly larvae, butterflies, larvae, fly larvae, insect larvae, arthropodlarvae, black soldier fly larvae, Hermetia illucens, antlions,mosquitos, Colorado potato beetle, Leptinotarsa decemlineata, moths,diamondback moth, Plutella xylostella, moth species of the familyPlutellidae and genus Plutella. Encarsia Formosa, insects in themacrolepidopteran clade Rhopalocera from the order Lepidoptera, whiteflyparasites, ladybugs, spiders, dragonflies, orb-weaving spiders,arachnids, Spodoptera frugiperda, members of the spider familyAraneidae, praying mantis, arachnids, eight-legged arthropods, andsix-legged arthropods.

In embodiments, the pet food is shaped, cooked, flavored as disclosedherein. In embodiments, the pet food is kibble, wet, or canned. Inembodiments, the pet food includes a water content ranging from between1 weight percent of water to 2 weight percent of water, 2 weight percentof water to 3 weight percent of water, 3 weight percent of water to 4weight percent of water, 4 weight percent of water to 5 weight percentof water, 5 weight percent of water to 6 weight percent of water, 6weight percent of water to 7 weight percent of water, 7 weight percentof water to 8 weight percent of water, 8 weight percent of water to 9weight percent of water, 9 weight percent of water to 10 weight percentof water, 10 weight percent of water to 11 weight percent of water, 11weight percent of water to 12 weight percent of water, 12 weight percentof water to 13 weight percent of water, 13 weight percent of water to 14weight percent of water, 14 weight percent of water to 15 weight percentof water, 15 weight percent of water to 16 weight percent of water, 16weight percent of water to 17 weight percent of water, 17 weight percentof water to 18 weight percent of water, 18 weight percent of water to 19weight percent of water, and 19 weight percent of water to 20 weightpercent of water, 20 weight percent of water to 25 weight percent ofwater, 25 weight percent of water to 30 weight percent of water, 30weight percent of water to 35 weight percent of water, 35 weight percentof water to 40 weight percent of water, 40 weight percent of water to 50weight percent of water, 50 weight percent of water to 60 weight percentof water, 60 weight percent of water to 65 weight percent of water, 65weight percent of water to 70 weight percent of water.

FIG. 19′

FIG. 19′ illustrates a single fully-grown DANLEO III plant.

FIG. 20′

FIG. 20′ illustrates zoomed-in view of a budding or flowering plant.

FIG. 21′

FIG. 21′ illustrates a single leaf of DANLEO III.

FIG. 22′

FIG. 22′ illustrates a trimmed and dried bud (reproductive structure) ofDANLEO III.

FIGS. 19′-22′ illustrate the overall appearance of the DANLEO III. Thesephotographs show the colors as true as it is reasonably possible toobtain in reproductions of this type. Colors in the photographs maydiffer slightly from the color values cited in the detailed botanicaldescription which accurately describe the colors of DANLEO III.

This disclosure relates to a new and distinct hybrid plant named DANLEOIII characterized by a mixture of Cannabis sativa L. ssp.Sativa×Cannabis sativa L. ssp. Indica (Lam.); Within the leaves, seeds,stems, roots, or any reproductive structures, DANLEO III has a:

-   (a) a cannabidiol content ranging from 0.125 weight percent to less    than 5 weight percent;-   (b) a tetrahydrocannabinol ranging from 5 weight percent to 63    weight percent;-   (c) an energy content ranging from between 2,500 British Thermal    Units per pound to 15,000 British Thermal Units per pound;-   (d) a carbon content ranging from between 20 weight percent to 65    weight percent;-   (e) an oxygen content ranging from between 12 weight percent to 55    weight percent;-   (f) a hydrogen content ranging from between 2 weight percent to 20    weight percent;-   (g) an ash content ranging from between 2.5 weight percent to 30    weight percent;-   (h) volatiles content ranging from between 30 weight percent to 90    weight percent;-   (i) a nitrogen content ranging from between 1 weight percent to 10    weight percent;-   (j) a sulfur content ranging from between 0.01 weight percent to 8    weight percent;-   (k) a chlorine content ranging from 0.05 weight percent to 5 weight    percent;-   (l) a sodium content ranging from 0.02 weight percent to 15 weight    percent;-   (m) a potassium content ranging from 0.05 weight percent to 15    weight percent;-   (n) an iron content ranging from 0.01 weight percent to 13 weight    percent;-   (o) a magnesium content ranging from 0.02 weight percent to 10    weight percent;-   (p) a phosphorous content ranging from 0.05 weight percent to 12    weight percent;-   (q) a calcium content ranging from 0.03 weight percent to 10 weight    percent;-   (r) a zinc content ranging from 0.01 weight percent to 5 weight    percent;-   (s) a cellulose content ranging from 25 weight percent to 75 weight    percent;-   (t) a lignin content ranging from 3 weight percent to 35 weight    percent;-   (u) a hemicellulose content ranging from 3 weight percent to 30    weight percent;-   (v) a fat content ranging from 5 weight percent to 35 weight    percent;-   (w) a fiber content ranging from 5 weight percent to 75 weight    percent; and-   (x) a protein content ranging from 5 weight percent to 35 weight    percent;    wherein:    the Cannabis Sativa L. ssp indica content ranges from 15% to 65%;    the Cannabis Sativa L. ssp sativa content ranges from 20% to 70%.

In embodiments, DANLEO III also includes: a N-acetylglucosamine contentranging from between: 0.050 parts per million to 0.100 parts permillion, 0.100 parts per million to 0.200 parts per million, 0.200 partsper million to 0.400 parts per million, 0.400 parts per million to 0.800parts per million, 0.800 parts per million to 1.600 parts per million,1.600 parts per million to 3.200 parts per million, 3.200 parts permillion to 6.400 parts per million, 6.4 parts per million to 12.8 partsper million, 12.8 parts per million to 25.6 parts per million, 25 partsper million to 50 parts per million, 50 parts per million to 100 partsper million, 100 parts per million to 200 parts per million, 200 partsper million to 400 parts per million, 400 parts per million to 800 partsper million, 800 parts per million to 1600 parts per million, 1600 partsper million to 3200 parts per million, 3200 parts per million to 6400parts per million, 6400 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, 14 weight percent to 15 weight percent, 15 weight percent to 16weight percent, 16 weight percent to 17 weight percent, 17 weightpercent to 18 weight percent, 18 weight percent to 19 weight percent, 19weight percent to 20 weight percent, 20 weight percent to 21 weightpercent, 21 weight percent to 22 weight percent, 22 weight percent to 23weight percent, 23 weight percent to 24 weight percent, 24 weightpercent to 25 weight percent, 25 weight percent to 30 weight percent, 30weight percent to 35 weight percent, 35 weight percent to 40 weightpercent, 40 weight percent to 45 weight percent, 45 weight percent to 50weight percent, 50 weight percent to 55 weight percent, 55 weightpercent to 60 weight percent, 60 weight percent to 65 weight percent, 65weight percent to 70 weight percent, 70 weight percent to 75 weightpercent, 75 weight percent to 80 weight percent, 80 weight percent to 85weight percent, 85 weight percent to 90 weight percent, 90 weightpercent to 95 weight percent, 95 weight percent to 95.25 weight percent,95.25 weight percent to 95.50 weight percent, 95.50 weight percent to95.75 weight percent, 95.75 weight percent to 96.00 weight percent,96.00 weight percent to 96.25 weight percent, 96.25 weight percent to96.50 weight percent, 96.50 weight percent to 96.75 weight percent,96.75 weight percent to 97.00 weight percent, 97.00 weight percent to97.25 weight percent, 97.25 weight percent to 97.50 weight percent,97.50 weight percent to 97.75 weight percent, 97.75 weight percent to98.00 weight percent, 98.00 weight percent to 98.25 weight percent,98.25 weight percent to 98.50 weight percent, 98.50 weight percent to98.75 weight percent, 98.75 weight percent to 99.00 weight percent,99.00 weight percent to 99.25 weight percent, 99.25 weight percent to99.50 weight percent, 99.50 weight percent to 99.75 weight percent, and99.75 weight percent to 99.99 weight percent.

In embodiments, DANLEO III also includes: a fungus content ranging frombetween: 0.050 parts per million to 0.100 parts per million, 0.100 partsper million to 0.200 parts per million, 0.200 parts per million to 0.400parts per million, 0.400 parts per million to 0.800 parts per million,0.800 parts per million to 1.600 parts per million, 1.600 parts permillion to 3.200 parts per million, 3.200 parts per million to 6.400parts per million, 6.4 parts per million to 12.8 parts per million, 12.8parts per million to 25.6 parts per million, 25 parts per million to 50parts per million, 50 parts per million to 100 parts per million, 100parts per million to 200 parts per million, 200 parts per million to 400parts per million, 400 parts per million to 800 parts per million, 800parts per million to 1600 parts per million, 1600 parts per million to3200 parts per million, 3200 parts per million to 6400 parts permillion, 6400 parts per million to 1 weight percent.

In embodiments, DANLEO III also includes: a bacteria content rangingfrom between: 0.05 colony-forming units per gram (CFU/g) to 0.100 CFU/g,0.1 CFU/g to 0.2 CFU/g, 0.2 CFU/g to 0.4 CFU/g, 0.4 CFU/g to 0.8 CFU/g,0.8 CFU/g to 1.6 CFU/g, 1.6 CFU/g to 3.2 CFU/g, 3.2 CFU/g to 6.4 CFU/g,6.4 CFU/g to 12.8 CFU/g, 12.8 CFU/g to 25 CFU/g, 25 CFU/g to 50 CFU/g,50 CFU/g to 100 CFU/g, 100 CFU/g to 200 CFU/g, 200 CFU/g to 400 CFU/g,400 CFU/g to 800 CFU/g, 800 CFU/g to 1,600 CFU/g, 1,600 CFU/g to 3,200CFU/g, 3,200 CFU/g to 6,400 CFU/g, 32,000 CFU/g to 320,000 CFU/g,320,000 CFU/g to 3,200,000 CFU/g, 3,200,000 CFU/g to 32,000,000 CFU/g.

In embodiments, DANLEO III also includes: a fungus content ranging frombetween: 0.05 colony-forming units per gram (CFU/g) to 0.100 CFU/g, 0.1CFU/g to 0.2 CFU/g, 0.2 CFU/g to 0.4 CFU/g, 0.4 CFU/g to 0.8 CFU/g, 0.8CFU/g to 1.6 CFU/g, 1.6 CFU/g to 3.2 CFU/g, 3.2 CFU/g to 6.4 CFU/g, 6.4CFU/g to 12.8 CFU/g, 12.8 CFU/g to 25 CFU/g, 25 CFU/g to 50 CFU/g, 50CFU/g to 100 CFU/g, 100 CFU/g to 200 CFU/g, 200 CFU/g to 400 CFU/g, 400CFU/g to 800 CFU/g, 800 CFU/g to 1,600 CFU/g, 1,600 CFU/g to 3,200CFU/g, 3,200 CFU/g to 6,400 CFU/g, 32,000 CFU/g to 320,000 CFU/g,320,000 CFU/g to 3,200,000 CFU/g, 3,200,000 CFU/g to 32,000,000 CFU/g.

In embodiments, DANLEO III also includes: an alanine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: an arginine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: an aspartic acid contentranging from between: 500 parts per million to 1000 parts per million,1000 parts per million to 5000 parts per million, 5000 parts per millionto 7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a glutamic acid contentranging from between: 500 parts per million to 1000 parts per million,1000 parts per million to 5000 parts per million, 5000 parts per millionto 7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a glycine content ranging frombetween: 500 parts per million to 1000 parts per million, 1000 parts permillion to 5000 parts per million, 5000 parts per million to 7500 partsper million, 7500 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a histidine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: an isoleucine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a Leucine content ranging frombetween: 500 parts per million to 1000 parts per million, 1000 parts permillion to 5000 parts per million, 5000 parts per million to 7500 partsper million, 7500 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a lysine content ranging frombetween: 500 parts per million to 1000 parts per million, 1000 parts permillion to 5000 parts per million, 5000 parts per million to 7500 partsper million, 7500 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a proline content ranging frombetween: 500 parts per million to 1000 parts per million, 1000 parts permillion to 5000 parts per million, 5000 parts per million to 7500 partsper million, 7500 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a serine content ranging frombetween: 500 parts per million to 1000 parts per million, 1000 parts permillion to 5000 parts per million, 5000 parts per million to 7500 partsper million, 7500 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a threonine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a tyrosine content rangingfrom between: 500 parts per million to 1000 parts per million, 1000parts per million to 5000 parts per million, 5000 parts per million to7500 parts per million, 7500 parts per million to 1 weight percent, 1weight percent to 2 weight percent, 2 weight percent to 3 weightpercent, 3 weight percent to 4 weight percent, 4 weight percent to 5weight percent, 5 weight percent to 6 weight percent, 6 weight percentto 7 weight percent, 7 weight percent to 8 weight percent, 8 weightpercent to 9 weight percent, 9 weight percent to 10 weight percent, 10weight percent to 11 weight percent, 11 weight percent to 12 weightpercent, 12 weight percent to 13 weight percent, 13 weight percent to 14weight percent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a valine content ranging frombetween: 500 parts per million to 1000 parts per million, 1000 parts permillion to 5000 parts per million, 5000 parts per million to 7500 partsper million, 7500 parts per million to 1 weight percent, 1 weightpercent to 2 weight percent, 2 weight percent to 3 weight percent, 3weight percent to 4 weight percent, 4 weight percent to 5 weightpercent, 5 weight percent to 6 weight percent, 6 weight percent to 7weight percent, 7 weight percent to 8 weight percent, 8 weight percentto 9 weight percent, 9 weight percent to 10 weight percent, 10 weightpercent to 11 weight percent, 11 weight percent to 12 weight percent, 12weight percent to 13 weight percent, 13 weight percent to 14 weightpercent, or 14 weight percent to 15 weight percent.

In embodiments, DANLEO III also includes: a pH ranging from between:6.00 to 6.05, 6.05 to 6.10, 6.10 to 6.15, 6.15 to 6.20, 6.20 to 6.25,6.25 to 6.30, 6.30 to 6.35, 6.35 to 6.40, 6.40 to 6.45, 6.45 to 6.50,6.50 to 6.55, 6.55 to 6.60, 6.60 to 6.65, 6.65 to 6.70, 6.70 to 6.75,6.75 to 6.80, 6.80 to 6.85, 6.85 to 6.90, 6.90 to 6.95, 6.95 to 7.00,7.00 to 7.05, 7.05 to 7.10, 7.10 to 7.15, 7.15 to 7.20, 7.20 to 7.25,7.25 to 7.30, 7.30 to 7.35, 7.35 to 7.40, 7.40 to 7.45, 7.45 to 7.50,7.50 to 7.55, 7.55 to 7.60, 7.60 to 7.65, 7.65 to 7.70, 7.70 to 7.75,7.75 to 7.80, 7.80 to 7.85, 7.85 to 7.90, 7.90 to 7.95, 7.95 to 8.00,8.00 to 8.05, 8.05 to 8.10, 8.10 to 8.15, 8.15 to 8.20, 8.20 to 8.25,8.25 to 8.30, 8.30 to 8.35, 8.35 to 8.40, 8.40 to 8.45, or 8.45 to 8.50.

In embodiments, DANLEO III also includes: a water activity (Aw) rangingfrom between: 0.05 to 0.1, 0.1 to 0.15, 0.15 to 0.2, 0.2 to 0.25, 0.25to 0.3, 0.3 to 0.35, 0.35 to 0.4, 0.4 to 0.45, 0.45 to 0.5, 0.5 to 0.6,or 0.6 to 0.7, 0.7 to 0.8, or 0.8 to 0.9.

The present plant was developed in the United States. In embodiments,the plant may be propagated from seed. In embodiments, the plant isasexually propagated using stem cuttings especially for large-scaleproduction. In embodiments, the stem cutting may be ground, shredded,smashed, milled, crushed, and blended into a slurry or a liquid or gelwith treated water and/or a hormone and then incubated in a firstgrowing medium in a cloning enclosure to develop roots. It is preferredthat the first growing medium includes a hormone and a gel and the gelincludes one or more selected from the group consisting of acacia, agar,agave, alginate, alginic acid, alginin, aluminum monostearate,arrowroot, bentonite, bovine-derived gelatin, carbomer,carboxymethylcellulose calcium, carboxymethylcellulose sodium,carboxymethylcellulose sodium 12, carboxymethylcellulose sodiumcellulose, carrageenan, collagen, colloidal silicon dioxide, cornstarch,dextrin, furcellaran, gelatin, glycerin, guar gum, honey, hydroxyethylcellulose, hydroxypropyl cellulose, hydroxypropyl methylcellulose,katakuri starch, locust bean gum, magma bentonite, magnesium aluminumsilicate, methylcellulose, microcrystalline cellulose, pectin,polyethylene oxide, polyvinyl alcohol, potato starch, povidone, psylliumhusks, purified bentonite, sago, silicon dioxide, sodium alginate,sorbitol, sugars, syrup, tapioca, tragacanth, vegan gelatin, vegetablegum, xanthan gum, and combinations thereof; and, wherein, the hormone iscomprised of one or more from the group consisting of auxins, cytokininsgibberellins, abscic acid, brassinosteroids, salicylic acid, jasmonates,plant peptide hormones, polyamines, nitric oxide, strigolactones, andtriacontanol.

The plant may be grown indoors, such as for example in a greenhouse,building, or other suitable indoor growing environment under controlledconditions. In embodiments, the plant is grown outdoors. The density ofthe plant ranges from 3.5 pounds per cubic foot to about 14.999 poundsper cubic foot or a ground bulk density ranging from between about 15pounds per cubic foot to about 50 pounds per cubic foot.

In embodiments, the plants undergoes a deliberately stressed trainingmethod, including: (a) providing a branch of a cannabis plant; (b) afterstep (a), squeezing and/or bending the branch; (c) after step (b),allowing the plant to heal. In embodiments, after step (b) and beforestep (c), inspecting the plant for tears in the outside plant tissue andoptionally taping the branch that was squeezed and/or bended.

Plant

Exposed Plant Structure: This is an aggressive annual, dioecious plant.The natural height at 6 months old for indoor growth is 40 inches to 120inches, and, and for outdoor growth is 50 inches to 160 inches. Adetailed list of characteristics follows:

Botanical Classification:

Mixture of Cannabis sativa L. ssp. Sativa×Cannabis sativa L. ssp. Indica(Lam.).

Percentages:

A new and distinct hybrid plant named DANLEO III, as illustrated anddescribed herein characterized by a mixture of:

(i) Cannabis Sativa L. ssp indica, and

(ii) Cannabis Sativa L. ssp sativa;

within the leaves, seeds, stems, roots, or any reproductive structures,DANLEO III has a:

-   (a) a cannabidiol content ranging from 0.125 weight percent to less    than 5 weight percent;-   (b) a tetrahydrocannabinol ranging from 5 weight percent to 63    weight percent;-   (c) an energy content ranging from between 2,500 British Thermal    Units per pound to 15,000 British Thermal Units per pound;-   (d) a carbon content ranging from between 20 weight percent to 65    weight percent;-   (e) an oxygen content ranging from between 12 weight percent to 55    weight percent;-   (f) a hydrogen content ranging from between 2 weight percent to 20    weight percent;-   (g) an ash content ranging from between 2.5 weight percent to 30    weight percent;-   (h) volatiles content ranging from between 30 weight percent to 90    weight percent;-   (i) a nitrogen content ranging from between 1 weight percent to 10    weight percent;-   (j) a sulfur content ranging from between 0.01 weight percent to 8    weight percent;-   (k) a chlorine content ranging from 0.05 weight percent to 5 weight    percent;-   (l) a sodium content ranging from 0.02 weight percent to 15 weight    percent;-   (m) a potassium content ranging from 0.05 weight percent to 15    weight percent;-   (n) an iron content ranging from 0.01 weight percent to 13 weight    percent;-   (o) a magnesium content ranging from 0.02 weight percent to 10    weight percent;-   (p) a phosphorous content ranging from 0.05 weight percent to 12    weight percent;-   (q) a calcium content ranging from 0.03 weight percent to 10 weight    percent;-   (r) a zinc content ranging from 0.01 weight percent to 5 weight    percent;-   (s) a cellulose content ranging from 25 weight percent to 75 weight    percent;-   (t) a lignin content ranging from 3 weight percent to 35 weight    percent;-   (u) a hemicellulose content ranging from 3 weight percent to 30    weight percent;-   (v) a fat content ranging from 5 weight percent to 35 weight    percent;-   (w) a fiber content ranging from 5 weight percent to 75 weight    percent; and-   (x) a protein content ranging from 5 weight percent to 35 weight    percent;    wherein:    the Cannabis Sativa L. ssp indica content ranges from 15% to 65%;    the Cannabis Sativa L. ssp sativa content ranges from 20% to 70%.    PROPAGATION: This plant may be perpetuated by stem cuttings. Seed    propagation is possible but not preferred due to lack of efficiency    when compared to asexual reproduction.    TIME TO INITIATE ROOTS IN SUMMER: about 4 to 20 days.    Plant Description: Annual, dioecious flowering shrub; multi-stemmed;    vigorous; freely branching; removal of the terminal bud enhances    lateral branch development.

In embodiments, the turgor pressure within the plants includes the forcewithin the cell that pushes the plasma membrane against the cell wall.In embodiments, the turgor pressure within the plants includes one ormore pressure ranges selected from the group consisting of: 0.5 bars to0.6 bars, 0.6 bars to 0.7 bars, 0.7 bars to 0.8 bars, 0.8 bars to 0.9bars, 0.9 bars to 1 bars, 1 bars to 1.1 bars, 1.1 bars to 1.2 bars, 1.2bars to 1.3 bars, 1.3 bars to 1.4 bars, 1.4 bars to 1.5 bars, 1.5 barsto 1.6 bars, 1.6 bars to 1.7 bars, 1.7 bars to 1.8 bars, 1.8 bars to 1.9bars, 1.9 bars to 2 bars, 2 bars to 2.1 bars, 2.1 bars to 2.2 bars, 2.2bars to 2.3 bars, 2.3 bars to 2.4 bars, 2.4 bars to 2.5 bars, 2.5 barsto 2.6 bars, 2.6 bars to 2.7 bars, 2.7 bars to 2.8 bars, 2.8 bars to 2.9bars, and 2.9 bars to 3 bars.

Mature Habit: Tap-rooted annual, with extensive fibrous root system,upright and much branched aerial portion of plant. The growth form ofall cloned plants was highly manipulated by systematic removal ofterminal buds, inducing a greater branching habit. Many petiole scars onstems from systematic removal of large shade leaves. In this habit,these are obviously very vigorous annual herbs.First Year Stems:

Shape: Round. Moderate to fine pubescence.

First year stem strength: Medium to Strong.

First year stem color:

In embodiments, the young stem has a color that is comprised of one ormore from the group consisting of: light green (144C), yellow (001A) oryellow green (001A), dark green (144A) with shades of yellow (001A),yellow orange (011A), orange (024A), orange red (033B), orange pink(027A), red (033A), dark purple red (046A), light red pink (039C), redpink (043C), dark pink red (045D), purple red (054A), light blue pink(055C), purple (058A), purple red (059D), blue pink (062A), light blueviolet (069C), violet blue (089A), violet (075A), dark violet (079A),blue violet (083D), blue (100A), dark blue (103A), light blue (104D),light green blue (110C), green blue (111A), grey blue (115C), green blue(125C), white (155A), orange brown (169A), brown (172A), brown purple(178A), orange pink (179D) (The Royal Horticultural Society ColourChart, 1995 Ed.).

In embodiments, the older stem has a color that is comprised of one ormore from the group consisting of: light green (144C), yellow (001A) oryellow green (001A), dark green (144A) with shades of yellow (001A),yellow orange (011A), orange (024A), orange red (033B), orange pink(027A), red (033A), dark purple red (046A), light red pink (039C), redpink (043C), dark pink red (045D), purple red (054A), light blue pink(055C), purple (058A), purple red (059D), blue pink (062A), light blueviolet (069C), violet blue (089A), violet (075A), dark violet (079A),blue violet (083D), blue (100A), dark blue (103A), light blue (104D),light green blue (110C), green blue (111A), grey blue (115C), green blue(125C), white (155A), orange brown (169A), brown (172A), brown purple(178A), orange pink (179D) (The Royal Horticultural Society ColourChart, 1995 Ed.).

Stem Diameter:

In embodiments, the stem diameter at the soil line is 1.05 inches to7.15 inches. In embodiments, the middle of plant average stem diameteris 0.2 inches to 1.5 inches.

In embodiments, the stem diameter at the soil line is 0.75 inches to 4inches. In embodiments, the middle of plant average stem diameter is 0.2inches to 1.5 inches.

In embodiments, the stem diameter at the soil line is 0.25 inches to 2inches. In embodiments, the middle of plant average stem diameter is 0.1inches to 0.75 inches.

Stem Height:

In embodiments, the stem height is 3 feet to 9 feet. In embodiments, thestem height is 3 feet to 9 feet. In embodiments, the stem height is 1.5feet to 4.5 feet. In embodiments, the stem height is 5.5 feet to 11.25feet. In embodiments, the stem height is 10 feet to 20 feet. Inembodiments, the stem height is 11 feet to 24.5 feet. In embodiments,the stem height is 18 feet to 32 feet.

Stem Strength:

In embodiments, lateral stems are strong but benefit from being stakedduring flowering. In embodiments, the stem has a hollow cross-section.In embodiments, the stem is ribbed having ribs that run parallel to thestem. In embodiments, the stem is hollow.

Internode Spacing:

In embodiments, from between 1.15 inches to 2 inches at the top half ofthe plant. In embodiments, from between 1.15 inches to 3.15 inches atthe bottom half of the plant. In embodiments, from between 0.75 inchesto 5 inches at the bottom half of the plant. In embodiments, frombetween 0.35 inches to 3.15 inches at the bottom half of the plant. Inembodiments, from between 0.35 inches to 4.15 inches at the bottom halfof the plant. In embodiments, from between 1.15 inches to 7.15 inches atthe bottom half of the plant. In embodiments, from between 2 inches to 9inches at the bottom half of the plant. In embodiments, from between 2inches to 9 inches at the bottom half of the plant.

Foliage Description:

Texture (upper and lower surfaces): Upper surface scabrid withnon-visible stiff hairs; lower surface more or less densely pubescent,covered with sessile glands.

Branch strength: Strong to medium to weak.

Branch description: In embodiments, branches may be short, dense withshort, broad leaflets. In embodiments, branches may be medium length,dense with long, broad or compact leaflets. In embodiments, lateralbranches off the main stem may be fine and of medium strength, theycontain few leaves with many bud sites extending up the branch. Inembodiments, branches may be long and sparse.

Leaf Arrangement: In embodiments, palmately compound (digitate) leaveswith 5 to 9 serrates leaflets per leaf. In embodiments, palmatelycompound (digitate) leaves with 3 to 7 serrates leaflets per leaf. Inembodiments, palmately compound (digitate) leaves with 7 to 11 serratesleaflets per leaf. In embodiments, palmately compound (digitate) leaveswith 3 to 11 serrates leaflets per leaf. In embodiments, palmatelycompound (digitate) leaves with 5 to 11 serrates leaflets per leaf. Inembodiments, the bottom two leaflets may be angled upwards at about a45-degree angle towards the middle leaflet. In embodiments, the bottomtwo leaflets extend out from the petiole at approximately 180 degrees.

Leaf width: In embodiments, the average leaf width ranges from between1.5 inches to 12 inches. In embodiments, the average leaf width rangesfrom between 1.5 inches to 3 inches. In embodiments, the average leafwidth ranges from between 1.5 inches to 4 inches. In embodiments, theaverage leaf width ranges from between 1.5 inches to 5 inches. Inembodiments, the average leaf width ranges from between 1.5 inches to 6inches. In embodiments, the average leaf width ranges from between 1.5inches to 7 inches. In embodiments, the average leaf width ranges frombetween 1.5 inches to 8 inches. In embodiments, the average leaf widthranges from between 1.5 inches to 10 inches.

Leaf length: In embodiments, the average leaf length ranges from between1.5 inches to 12 inches. In embodiments, the average leaf length rangesfrom between 1.5 inches to 3 inches.

In embodiments, the average leaf length ranges from between 1.5 inchesto 4 inches. In embodiments, the average leaf length ranges from between1.5 inches to 5 inches. In embodiments, the average leaf length rangesfrom between 1.5 inches to 6 inches. In embodiments, the average leaflength ranges from between 1.5 inches to 7 inches. In embodiments, theaverage leaf length ranges from between 1.5 inches to 8 inches. Inembodiments, the average leaf length ranges from between 1.5 inches to10 inches.

Leaf venation pattern: Venation of each leaf is palmately compound(digitate), with serrated leaflets. In embodiments, the lateral venationextends off the main vein to each serrated tip. In embodiments, thesublateral veins extend to the notch of each serration rather than thetip. In embodiments, each serration has a lateral vein extending to itstip from the central (primary) vein of the leaflet. In embodiments, thefrom each lateral vein there is usually a single spur vein (sublateralvein) extending to the notch of each serration.

Leaf venation Color: Leaf venation is very colorful with one or morefrom the group consisting of: light green (144C), dark green (144A),yellow (001A), yellow orange (011A), orange (024A), orange red (033B),orange pink (027A), red (033A), dark purple red (046A), light red pink(039C), red pink (043C), dark pink red (045D), purple red (054A), lightblue pink (055C), purple (058A), purple red (059D), blue pink (062A),light blue violet (069C), violet blue (089A), violet (075A), dark violet(079A), blue violet (083D), blue (100A), dark blue (103A), light blue(104D), light green blue (110C), green blue (111A), grey blue (115C),green blue (125C), green (130A), dark green (132A), light green (149B),white (155A), orange brown (169A), brown (172A), brown purple (178A),orange pink (179D) (The Royal Horticultural Society Colour Chart, 1995Ed.).

Petiole length: Average length of petiole of fan leaves 1.5 inches to 8inches. In embodiments, Petioles are very study and appear a light brown(166C) or light green (144C) (The Royal Horticultural Society ColourChart, 1995 Ed.). Petioles are very study.

Petiole Color: Petioles are very colorful with one or more from thegroup consisting of: light green (144C), dark green (144A), yellow(001A), yellow orange (011A), orange (024A), orange red (033B), orangepink (027A), red (033A), dark purple red (046A), light red pink (039C),red pink (043C), dark pink red (045D), purple red (054A), light bluepink (055C), purple (058A), purple red (059D), blue pink (062A), lightblue violet (069C), violet blue (089A), violet (075A), dark violet(079A), blue violet (083D), blue (100A), dark blue (103A), light blue(104D), light green blue (110C), green blue (111A), grey blue (115C),green blue (125C), green (130A), dark green (132A), light green (149B),white (155A), orange brown (169A), brown (172A), brown purple (178A),orange pink (179D) (The Royal Horticultural Society Colour Chart, 1995Ed.).

Color of emerging foliage (upper surface): In embodiments, the color ofemerging foliage is have a color comprised of one or more from the groupconsisting of: light green (144C), dark green (144A), yellow (001A),yellow orange (011A), orange (024A), orange red (033B), orange pink(027A), red (033A), dark purple red (046A), light red pink (039C), redpink (043C), dark pink red (045D), purple red (054A), light blue pink(055C), purple (058A), purple red (059D), blue pink (062A), light blueviolet (069C), violet blue (089A), violet (075A), dark violet (079A),blue violet (083D), blue (100A), dark blue (103A), light blue (104D),light green blue (110C), green blue (111A), grey blue (115C), green blue(125C), green (130A), dark green (132A), light green (149B), white(155A), orange brown (169A), brown (172A), brown purple (178A), orangepink (179D) (The Royal Horticultural Society Colour Chart, 1995 Ed.).

Vegetative bud (reproductive structure) description: In embodiments, thedried flower buds (reproductive structures) are a light green (144C),green (124A), or dark green (144A), small to large in nature, diffuseand airy, and coated with glandular trichomes. In embodiments, thefragrance may be quite spicy with an earthy aroma with noticeable hintsof pine, clove, citrus, pepper, candy, and tropical fruit. Inembodiments, the fragrance is slightly sweet, having a fruity, fresh,musky, cotton-candy, or grape-soda type smell.

Flower description: In embodiments, inflorescence (buds, or reproductivestructures) may be conical, spherical, cylindrical, tubular, oblong, orrectangular. In embodiments, the flower, bud, or reproductive structuresmay be devoid of any petals. In embodiments, the flower, bud, orreproductive structures are comprised of a cluster of false spikes withsingle flowers. These flowers are often paired and enclosed by abracteole. In embodiments, the wet flower buds have a color comprised ofone or more from the group consisting of: light green (144C), dark green(144A), yellow (001A), yellow orange (011A), orange (024A), orange red(033B), orange pink (027A), red (033A), dark purple red (046A), lightred pink (039C), red pink (043C), dark pink red (045D), purple red(054A), light blue pink (055C), purple (058A), purple red (059D), bluepink (062A), light blue violet (069C), violet blue (089A), violet(075A), dark violet (079A), blue violet (083D), blue (100A), dark blue(103A), light blue (104D), light green blue (110C), green blue (111A),grey blue (115C), green blue (125C), green (130A), dark green (132A),light green (149B), white (155A), orange brown (169A), brown (172A),brown purple (178A), orange pink (179D) (The Royal Horticultural SocietyColour Chart, 1995 Ed.). In embodiments, the wet flower buds have manylong white (155A) pistils (hairs), which may become brown (172A) a weekbefore harvest (The Royal Horticultural Society Colour Chart, 1995 Ed.).

Seed description: In embodiments, the seeds typically brown (172A). Inembodiments, the seeds are brown (172A) and have stripes that includeone or more colors from the group consisting of light green (144C), darkgreen (144A), yellow (001A), yellow orange (011A), orange (024A), orangered (033B), orange pink (027A), red (033A), dark purple red (046A),light red pink (039C), red pink (043C), dark pink red (045D), purple red(054A), light blue pink (055C), purple (058A), purple red (059D), bluepink (062A), light blue violet (069C), violet blue (089A), violet(075A), dark violet (079A), blue violet (083D), blue (100A), dark blue(103A), light blue (104D), light green blue (110C), green blue (111A),grey blue (115C), green blue (125C), green (130A), dark green (132A),light green (149B), white (155A), orange brown (169A), brown (172A),brown purple (178A), orange pink (179D) (The Royal Horticultural SocietyColour Chart, 1995 Ed.). In embodiments, the wet flower buds have manylong white (155A) pistils (hairs), which may become brown (172A) a weekbefore harvest (The Royal Horticultural Society Colour Chart, 1995 Ed.).In embodiments, the seeds are on average about 0.1 inches to 0.2 inchesin diameter. In embodiments, the seeds are on average about 0.075 inchesto 0.4 inches in diameter. The seeds have a high fat content rangingfrom 4 weight percent to 45 weight percent, with an energy contentranging up to or less than 65,000 British Thermal Units per pound.

Vegetative bud (reproductive structure) color: In embodiments, the driedflower buds are very colorful and are comprised of a vast array ofdifferent colors including one or more from the group consisting oflight green (144C), green (124A), dark green (144A), yellow (001A),yellow orange (011A), orange (024A), orange red (033B), orange pink(027A), red (033A), dark purple red (046A), light red pink (039C), redpink (043C), dark pink red (045D), purple red (054A), light blue pink(055C), purple (058A), purple red (059D), blue pink (062A), light blueviolet (069C), violet blue (089A), violet (075A), dark violet (079A),blue violet (083D), blue (100A), dark blue (103A), light blue (104D),light green blue (110C), green blue (111A), grey blue (115C), green blue(125C), white (155A), orange brown (169A), brown (172A), brown purple(178A), orange pink (179D), (The Royal Horticultural Society ColourChart, 1995 Ed.).

Vegetative bud (reproductive structure) & pistils color: In embodiments,the dried flower buds (including reproductive structures) are comprisedof one or more from the group consisting of: green (144C or 144A) withyellow (001A) pistils, green (144C or 144A) with yellow orange (011A)pistils, green (144C or 144A) with orange (024A) pistils, green (144C or144A) with orange red (033B) pistils, green (144C or 144A) with orangepink (027A) pistils, green (144C or 144A) with red (033A) pistils, green(144C or 144A) with dark purple red (046A) pistils, green (144C or 144A)with light red pink (039C) pistils, green (144C or 144A) with red pink(043C) pistils, green (144C or 144A) with dark pink red (045D) pistils,green (144C or 144A) with purple red (054A) pistils, green (144C or144A) with light blue pink (055C) pistils, green (144C or 144A) withpurple (058A) pistils, green (144C or 144A) with purple red (059D)pistils, green (144C or 144A) with blue pink (062A) pistils, green (144Cor 144A) with light blue violet (069C) pistils, green (144C or 144A)with violet blue (089A) pistils, green (144C or 144A) with violet (075A)pistils, green (144C or 144A) with dark violet (079A) pistils, green(144C or 144A) with blue violet (083D) pistils, green (144C or 144A)with blue (100A) pistils, green (144C or 144A) with dark blue (103A)pistils, green (144C or 144A) with light blue (104D) pistils, green(144C or 144A) with light green blue (110C) pistils, green (144C or144A) with green blue (111A) pistils, green (144C or 144A) with greyblue (115C) pistils, green (144C or 144A) with green (124A) pistils,green (144C or 144A) with green blue (125C) pistils, green (144C or144A) with green (130A) pistils, green (144C or 144A) with dark green(132A) pistils, green (144C or 144A) with light green (149B) pistils,green (144C or 144A) with white (155A) pistils, green (144C or 144A)with orange brown (169A) pistils, green (144C or 144A) with brown (172A)pistils, green (144C or 144A) with brown purple (178A) pistils, green(144C or 144A) with orange pink (179D) (The Royal Horticultural SocietyColour Chart, 1995 Ed.).

Bud (reproductive structures) length: In embodiments, the bud spikelength ranges from 0.75 inches to 10 inches. In embodiments, the budspike length ranges from 0.75 inches to 20 inches. In embodiments, thebud spike length ranges from 0.75 inches to 30 inches. In embodiments,the bud spike length ranges from 0.75 inches to 40 inches.

Bud (reproductive structures) diameter: Flower size is approximately:0.25 inches to 3 inches in diameter; and approximately 0.35 to 10 inchesin height.

Flowering time: In embodiments, flowering time ranges from 5 weeks to 18weeks. In embodiments, flowering time ranges from 5 weeks to 28 weeks.In embodiments, flowering time ranges from 25 weeks to 37 weeks. Inembodiments, flowering time ranges from 35 weeks to 60 weeks. Inembodiments, flowering time ranges from 45 weeks to 101 weeks.

Peduncles: Peduncle strength is weak to medium to strong. Inembodiments, they can bend horizontally from weight of flower buds. Inembodiments, the average diameter of the peduncles ranges from between0.2 to 0.5 inches in diameter. In embodiments, the average diameter ofthe peduncles ranges from between 0.1 to 0.3 inches in diameter. Inembodiments, the average diameter of the peduncles ranges from between0.3 to 1 inches in diameter. In embodiments, the average diameter of thepeduncles ranges from between 1 to 2 inches in diameter. In embodiments,texture is smooth with few hairs. In embodiments, texture is moderatelysmooth, glabrous. In embodiments, texture is coarse with many hairs. Inembodiments, pedicels are short to medium length, with visible hairs.They may be scabrid with sessile glands. In embodiments, pedicels areshort to medium length, scabrid with sessile glands and visible hairs.

Peduncles color: In embodiments, peduncles are very colorful with manyvaried colors including having one or more from the group selected from:light green (144C), dark green (144A), yellow (001A), yellow orange(011A), orange (024A), orange red (033B), orange pink (027A), red(033A), dark purple red (046A), light red pink (039C), red pink (043C),dark pink red (045D), purple red (054A), light blue pink (055C), purple(058A), purple red (059D), blue pink (062A), light blue violet (069C),violet blue (089A), violet (075A), dark violet (079A), blue violet(083D), blue (100A), dark blue (103A), light blue (104D), light greenblue (110C), green blue (111A), grey blue (115C), green blue (125C),green (130A), dark green (132A), light green (149B), white (155A),orange brown (169A), brown (172A), brown purple (178A), orange pink(179D) (The Royal Horticultural Society Colour Chart, 1995 Ed.).

Pedicel color: Pedicels are very colorful with many varied colorsincluding having one or more from the group selected from: light green(144C), dark green (144A), yellow (001A), yellow orange (011A), orange(024A), orange red (033B), orange pink (027A), red (033A), dark purplered (046A), light red pink (039C), red pink (043C), dark pink red(045D), purple red (054A), light blue pink (055C), purple (058A), purplered (059D), blue pink (062A), light blue violet (069C), violet blue(089A), violet (075A), dark violet (079A), blue violet (083D), blue(100A), dark blue (103A), light blue (104D), light green blue (110C),green blue (111A), grey blue (115C), green blue (125C), green (130A),dark green (132A), light green (149B), white (155A), orange brown(169A), brown (172A), brown purple (178A), orange pink (179D) (The RoyalHorticultural Society Colour Chart, 1995 Ed.).

Seed production on this plant is difficult. Seed production can beinduced using colloidal silver solution but even with this step maleinflorescence production is marginal. Pollen generated from thisprocedure may then be collected and used to self-cross with anon-treated female. The relative proportion of male plants ismedium/high.

The inflorescences (e.g.—flowers, buds, reproductive structures) of thefemale plant are used for medical purposes. This plant is veryversatile. It can be used to treat a wide range of health disorders. Ithas many beneficial medicinal qualities. Some uses include: stimulant,anti-inflammatory, pain management, sleep disorders, Tourette syndrome,Parkinson's disease, spasms, post-traumatic stress disorder (PTSD),epilepsy, multiple sclerosis, digestive disorders,

DANLEO III prefers water having an electrical conductivity ranging from0.10 microsiemens per centimeter to 100 microsiemens per centimeter.Other water sources with other electrical conductivity may be suitablebut just not as efficient. DANLEO III prefers water having an electricalconductivity ranging from 0.10 microsiemens per centimeter to 100microsiemens per centimeter is provided by:

(a1) a first water treatment unit (A1) including a cation,

(a2) a second water treatment unit (A2) including an anion, and

(a3) a third water treatment unit (A3) including a membrane.

In embodiments, DANLEO III is grown using a method by providing waterhaving an electrical conductivity ranging from 0.10 microsiemens percentimeter to 100 microsiemens per centimeter, the method includes:

-   -   (a) providing:

(a1) a first water treatment unit (A1) including a cation configured toremove positively charged ions from water to form a positively chargedion depleted water (06A), the positively charged ions are comprised ofone or more from the group consisting of calcium, magnesium, sodium, andiron;

(a2) a second water treatment unit (A2) including an anion configured toremove negatively charged ions from the positively charged ion depletedwater (06A) to form a negatively charged ion depleted water (09A), thenegatively charged ions are comprised of one or more from the groupconsisting of iodine, chloride, and sulfate;

(a3) a third water treatment unit (A3) including a membrane configuredto remove undesirable compounds from the negatively charged ion depletedwater (09A) to form an undesirable compounds depleted water (12A), theundesirable compounds are comprised of one or more from the groupconsisting of dissolved organic chemicals, viruses, bacteria, andparticulates;

-   -   (b) providing a source of water;    -   (c) removing positively charged ions from the water of step (b)        to form a positively charged ion depleted water;    -   (d) removing negatively charged ions from the water after        step (c) to form a negatively charged ion depleted water;    -   (e) removing undesirable compounds from the water after step (d)        to form an undesirable compound depleted water;    -   (f) mixing the undesirable compounds depleted water after        step (e) with one or more from the group consisting of        macro-nutrients, micro-nutrients, and a pH adjustment to form a        liquid mixture;    -   (g) pressurizing the liquid mixture of step (f) to form a        pressurized liquid mixture;    -   (h) splitting the pressurized liquid mixture into a plurality of        pressurized liquid mixtures;    -   (i) transferring the plurality of pressurized liquid mixtures to        each growing assembly;    -   wherein:        -   the macro-nutrients are comprised of one or more from the            group consisting of nitrogen, phosphorus, potassium,            calcium, magnesium, and sulfur;        -   the micro-nutrients are comprised of one or more from the            group consisting of iron, manganese, boron, molybdenum,            copper, zinc, sodium, chlorine, and silicon;        -   the pH adjustment solution is comprised of one or more from            the group consisting acid, nitric acid, phosphoric acid,            potassium hydroxide, sulfuric acid, organic acids, citric            acid, and acetic acid.

This new and remarkable variety of plant prefers that lights illuminatethe plant at an illumination on-off ratio ranging from between 0.5 and5, the illumination on-off ratio is defined as the duration of time whenthe lights are on and illuminate the plant in hours divided by thesubsequent duration of time when the lights are off and are notilluminating the plant in hours before the lights are turned on again.In embodiments, this variety of plant thrives at a carbon dioxideconcentration that between 400 parts per million (ppm) to 500 ppm, 500ppm to 600 ppm, 600 ppm to 700 ppm, 700 ppm to 800 ppm, 800 ppm to 900ppm, 900 ppm to 1000 ppm, 1000 ppm to 1500 ppm, 1500 ppm to 2000 ppm,2000 ppm to 2500 ppm, 2500 ppm to 3000 ppm, 3000 ppm to 3500 ppm, 3500ppm to 4000 ppm, 4000 ppm to 4500 ppm, 4500 ppm to 5000 ppm, 5000 ppm to5500 ppm, 5500 ppm to 6000 ppm, 6000 ppm to 6500 ppm, 6500 ppm to 7000ppm, 7000 ppm to 7500 ppm, 7500 ppm to 8000 ppm, 8000 ppm to 8500 ppm,8500 ppm to 9000 ppm, 9000 ppm to 9500 ppm, or 9500 ppm to 10000 ppm.

In embodiments, the DANLEO III is grown in a farming superstructuresystem (FSS) as described here and is grown while the FSS system isoperated in a manner that switches from one mode of operation to anothermode of operation.

In embodiments, the farming superstructure system (FSS) is operated in amanner that switches on a cyclical basis from: a first mode of operationto the second mode of operation; a second mode of operation to the firstmode of operation. In embodiments, the farming superstructure system(FSS) is operated in a manner that switches on a cyclical basis from: athird mode of operation to the fourth mode of operation; a fourth modeof operation to the third mode of operation. It is preferred to turn onand off at least one valves (V1, V3, V4) in a cyclical manner to preventthe roots of the cannabis from receiving too much mist or spray orliquid water or water or nutrients.

In embodiments, the first mode of operation lasts for 5 seconds openfollowed by the second mode of operation lasting for 600 seconds closed.In embodiments, the third mode of operation lasts for 5 seconds openfollowed by the fourth mode of operation lasting for 600 seconds closed.In embodiments, water is transferred to the first growing assembly (100)for 5 seconds followed by not transferring water to the first growingassembly (100) for 600 seconds. In embodiments, water is transferred tothe second growing assembly (200) for 5 seconds followed by nottransferring water to the second growing assembly (200) for 600 seconds.In embodiments, water is transferred to both the first and secondgrowing assemblies (100, 200) for 5 seconds followed by not transferringwater to both the first and second growing assemblies (100, 200) for 600seconds. 5 divided by 600 is 0.008.

In embodiments, the first mode of operation lasts for 60 seconds openfollowed by the second mode of operation lasting for 180 seconds closed.In embodiments, the third mode of operation lasts for 60 seconds openfollowed by the fourth mode of operation lasting for 180 seconds closed.In embodiments, water is transferred to the first growing assembly (100)for 60 seconds followed by not transferring water to the first growingassembly (100) for 180 seconds. In embodiments, water is transferred tothe second growing assembly (200) for 60 seconds followed by nottransferring water to the second growing assembly (200) for 180 seconds.60 divided by 180 is 0.333.

The duration of time when liquid is transferred to at least one growingassembly (100, 200) divided by the duration of time when liquid is nottransferred to at least one growing assembly (100, 200) may beconsidered an open-close ratio. The open-close ratio may be the durationof time when at least one valve (V1, V3, V4) is open in seconds dividedby the subsequent duration of time when the same valve is closed inseconds before the same valve opens again. In embodiments, theopen-close ratio ranges from between 0.008 to 0.33. In embodiments, thecomputer (COMP) opens and closes the valve (V1, V3, V4) to periodicallyintroduce the pressurized liquid mixture into to each growing assemblywith an open-close ratio ranging from between 0.008 to 0.33, theopen-close ratio is defined as the duration of time when the valve (V1,V3, V4) is open in seconds divided by the subsequent duration of timewhen the same valve is closed in seconds before the same valve opensagain. The computer (COMP) opens and closes the valves (V1, V3, V4) toperiodically introduce the pressurized liquid mixture into to eachgrowing assembly with an open-close ratio ranging from between 0.008 to0.33.

In embodiments, the open-close ratio varies. The open-close ratio mayvary throughout the life of the cannabis contained within the growingassemblies (100, 200). The open-close ratio may vary throughout thestage of development of the cannabis contained within the growingassemblies (100, 200). Stages of development of the cannabis includeflowering, pollination, fertilization. In embodiments, the open-closeratio is greater during flowering and less during pollination. Inembodiments, the open-close ratio is greater during pollination and lessduring fertilization. In embodiments, the open-close ratio is greaterduring flowering and less during fertilization. In embodiments, theopen-close ratio is less during flowering and greater duringpollination. In embodiments, the open-close ratio is less duringpollination and greater during fertilization. In embodiments, theopen-close ratio is less during flowering and greater duringfertilization.

The open-close ratio may vary throughout a 24-hour duration of time. Inembodiments, the open-close ratio is increased during the day-time anddecreased during the night-time relative to one another. In embodiments,the open-close ratio varies increased during the night-time anddecreased during the day-time relative to one another. Night-time isdefined as the time between evening and morning. Day-time is defined asthe time between morning and evening.

In embodiments, carbohydrates may be made available to DANLEO III. Thecarbohydrates are comprised of one or more from the group consisting ofsugar, sucrose, molasses, and plant syrups.

In embodiments, enzymes may be made available to DANLEO III. The enzymesare comprised of one or more from the group consisting of amino acids,orotidine 5′-phosphate decarboxylase, OMP decarboxylase, glucanase,beta-glucanase, cellulase, xylanase, HYGROZYME®, CANNAZYME®, MICROZYME®,and SENSIZYME®.

In embodiments, vitamins may be made available to DANLEO III. Thevitamins are comprised of one or more from the group consisting ofvitamin B, vitamin C, vitamin D, and vitamin E.

In embodiments, hormones may be made available to DANLEO III. Thehormones are comprised of one or more from the group consisting ofauxins, cytokinins gibberellins, abscic acid, brassinosteroids,salicylic acid, jasmonates, plant peptide hormones, polyamines, nitricoxide, strigolactones, and triacontanol.

In embodiments, microorganisms may be made available to DANLEO III. Themicroorganisms are comprised of one or more from the group consisting ofbacteria, diazotroph bacteria, diazotrop archaea, azotobactervinelandii, clostridium pasteurianu, fungi, arbuscular mycorrhizalfungi, glomus aggrefatum, glomus etunicatum, glomus intraradices,rhizophagus irregularis, and glomus mosseae.

Permits and Patent Licenses are Required for Growth of Danleo III in theUnited States of America and Internationally.

The claims and specification are in conformity with 37 CFR 1.163, thisspecification and especially claimed ranges of elements (a) through (x)and other elements of the claims contain as full and complete adisclosure as possible of the plant and the characteristics thereof thatdistinguish the same over related known varieties, and its antecedents,and particularly point out where and in what manner the variety of planthas been asexually reproduced. Further, in the case of this newly foundplant, this specification particularly points out the location andcharacter of the area where the plant was discovered. Applicant is basedout of Baltimore, Md., 21202.

The claims and specification are in conformity with 35 U.S.C. 112(a),since this specification and especially claimed ranges of elements (a)through (x) and other elements of the claims contain a writtendescription of the invention, and of the manner and process of makingand using it, in such full, clear, concise, and exact terms as to enableany person skilled in the art to which it pertains, or with which it ismost nearly connected, to make and use the same, and shall set forth thebest mode contemplated by the inventor or joint inventor of carrying outthe invention.

Complete botanical description and the characteristics which distinguishover related known varieties are herein provided. The new varietydiffers from parents and related (similar) cultivars of Cannabis sativaL. ssp. Sativa and Cannabis sativa L. ssp. Indica (Lam.). The newvariety differs from parents and related (similar) cultivars becauseDANLEO III has a precise and unique engineered concentrations of:cannabidiol, tetrahydrocannabinol, energy, carbon, oxygen, hydrogen,ash, volatiles, nitrogen, sulfur, chlorine, sodium, potassium, iron,magnesium, phosphorous, calcium, zinc, cellulose, lignin, hemicellulose,fat, fiber, protein, as well as specific Cannabis sativa L. ssp. Sativaand Cannabis sativa L. ssp. Indica (Lam.) contents and ratios. The newplant differs from its parents and related cultivars because it isengineered to more effectively alleviate inflammation, manage pain,treat post-traumatic stress disorder (PTSD), and digestive disorders,while also helping to prevent sleep disorders. It provides adequatestimulant to cure attention deficit disorder but does not so act as sucha stimulating drug to prevent normal sleep, dietary, and exercisepatterns. Because of this remarkable new plant, and combination ofingredients, individuals seeking to medicate with tetrahydrocannabinolcan now use this plant as medicine while having little-to-no sideeffects at all whatsoever and at a very low dosage compared to itsparents and related cultivars.

Applicant has specifically identified the characteristic of improvedmedicinal benefits through extensive trial and error and has a claimwhich is the result of quantifiable, experimental, and empirical datacharacterizing the difference between DANLEO III and Cannabis sativa L.ssp. Sativa or Cannabis sativa L. ssp. Indica (Lam.) alone. Mostimportantly, DANLEO III possesses a volatiles content ranging frombetween 30 weight percent to 90 weight percent, and a Cannabis sativa L.ssp. Sativa content ranges from 20 weight percent to 70 weight percent,and a Cannabis sativa L. ssp. Indica (Lam.) content ranges from 15weight percent to 65 weight percent. Whereas the patents and cultivarspossess 100 weight percent of each of Cannabis sativa L. ssp. Sativacontent and a Cannabis sativa L. ssp. Indica (Lam.), applicant'sresearch and development has resulted in a new and distinct plant thathas an engineered amount of volatiles while mixing Cannabis sativa L.ssp. Sativa content and a Cannabis sativa L. ssp. Indica (Lam.) atvarying ratios to achieve a preferred cannabidiol content ranging from0.125 weight percent to 25 weight percent. Applicant has realized thatthe tetrahydrocannabinol content ranging from 5 weight percent to 63weight percent is specifically tailored to maximize dosage while havinga volatiles content ranging from between 30 weight percent to 90 weightpercent. The combination of DANLEO III having a volatiles contentranging from between 30 weight percent to 90 weight percent togetherwith the tetrahydrocannabinol content ranging from 5 weight percent to63 weight percent provides a remarkable new plant. Because of this, auser can use less of the plant to achieve the required dosage.

The application conforms to 37 CFR 1.163(a) since the specificationparticularly points out that Applicant is based out of Baltimore, Md.,USA in zip code 21202 which was the location that Applicant realizedthat he can take stem cuttings and asexually reproduce plants in amanner disclosed in this specification. This disclosure conforms to 37CFR 1.163(a) since the specification particularly points out thatBaltimore, Md., USA in zip code 21202, indoor propagation, growing, andcultivation were the location and character of the area where the plantwas discovered.

Applicant has generated the ranges of claimed ranges of elements (a)through (x) were discovered through comprehensive compositionalanalysis, particle-induced X-ray emission analysis, elemental analysis,proximate analysis, and ultimate analysis immediately available from avariety of different laboratories in the USA. Obtaining the appropriateranges of varying concentrations of Cannabis sativa L. ssp. Sativa andCannabis sativa L. ssp. Indica (Lam.) were performed on a trial anderror basis. The tetrahydrocannabinol concentration is provided as ameasurement of DANLEO III's leaves, seeds, stems, roots, or anyreproductive structures on a dry basis.

The age and growing conditions of this plant shown in FIGS. 1-4 may be:adult plant of 14 weeks, average temperature 70 degrees F. to 80 degreesF., humidity 45 to 55 percent humidity, water pH from 5.15 to 6.8, waterhaving an electrical conductivity ranging from 0.10 microsiemens percentimeter to 100 microsiemens per centimeter, an illumination on-offratio ranging from between 0.5 and 5 (the illumination on-off ratio isdefined as the duration of time when the lights are on and illuminatethe cannabis in hours divided by the subsequent duration of time whenthe lights are off and are not illuminating the cannabis in hours beforethe lights are turned on again), a carbon dioxide concentration that isgreater than 400 parts per million and less than 3,000 parts permillion, a LED lighting wavelength ranging from 400 nm to 700 nm, airvelocity ranging from 5 feet per second to 50 feet per second.

The parents of the instant plant are known and are comprised of Cannabissativa L. ssp. Sativa×Cannabis sativa L. ssp. Indica (Lam.). Seeds fromeither are commercially available from many vendors throughout the USA.Applicant devised various plant hybrids of Cannabis sativa L. ssp.Sativa×Cannabis sativa L. ssp. Indica (Lam.) to create a plant bestsuited to accommodate industrial, commercial, recreation and medicinalpopular demand.

The idea of a superior and precisely engineered composition thatembodies DANLEO III as described and disclosed herein was discovered bythe applicant's in his garden where the inventor was asexuallyreproducing and cultivating many plants, in many different containers,of many different species. Applicant's work with plants has resulted inthe discovery of a cross between Cannabis sativa L. ssp. Sativa×Cannabissativa L. ssp. Indica (Lam.) described herein. Applicant has discoveredthat DANLEO III can be reproduced asexually, by taking cuttings of theplants of origin resulting in a remarkable new plant. The discoveredfemale plant can be asexually reproduced by cuttings.

The invention employs a novel plant variety. Since the plant isessential to the claimed invention it must be obtainable by thefollowing method. A method to asexually clone a plurality of DANLEO IIIplants, the method includes:

-   -   (a) providing:        -   (a0) a plurality of DANLEO III (107, 207) plants;        -   (a1) a cutting tool (CT1);        -   (a2) a liquid, powder, or gel rooting solution (RS), the            rooting solution includes one or more from the group            consisting of water, carbohydrates, enzymes, vitamins,            hormones, and microorganisms;        -   (a3) a growing medium (GM), the growing medium includes one            or more from the group consisting of rockwool, perlite,            amorphous volcanic glass, vermiculite, clay, clay pellets,            LECA (lightweight expanded clay aggregate), coco-coir,            fibrous coconut husks, soil, dirt, peat, peat moss, sand,            soil, compost, manure, fir bark, foam, gel, oasis cubes,            lime, gypsum, quartz, plastic, polyethylene, high-density            polyethylene (HDPE), low-density polyethylene (LDPE),            polyethylene terephthalate (PET), polyacrylonitrile, and            polypropylene; and        -   (a4) a plurality of containers (TY1, TY2, TY3, TY^(N),            TY^(N+1)) configured to accept the rooting solution (RS) and            the growing medium (GM), the plurality of containers are            configured to be positioned within a cloning enclosure            (CHD);        -   (a5) the cloning enclosure (CHD) has an interior (CHD-1),            the cloning enclosure (CHD) is configured to contain water            vapor within the interior (CHD-1) to provide a humid            environment for plants within the interior (CHD-1);    -   (b) introducing the rooting solution and the growing medium to        the plurality of containers;    -   (c) using the cutting tool to sever the tips from a plurality of        DANLEO III plants to form a plurality of severed plants (107X,        207X);    -   (d) inserting the plurality of severed plants (107X, 207X) of        step (c) into the plurality of containers;    -   (e) placing the plurality of containers within the interior of        the cloning enclosure;    -   (f) illuminating the plants after step (e);    -   (g) growing the plants for 4 to 20 days or until roots are        formed; and    -   (h) optionally venting the interior of the cloning enclosure;

wherein:

the carbohydrates are comprised of one or more from the group consistingof sugar, sucrose, molasses, and plant syrups;

the enzymes are comprised of one or more from the group consisting ofamino acids, orotidine 5′-phosphate decarboxylase, OMP decarboxylase,glucanase, beta-glucanase, cellulase, xylanase, HYGROZYME®, CANNAZYME®,MICROZYME®, and SENSIZYME®;

the vitamins are comprised of one or more from the group consisting ofvitamin B, vitamin C, vitamin D, and vitamin E;

the hormones are comprised of one or more from the group consisting ofauxins, cytokinins gibberellins, abscic acid, brassinosteroids,salicylic acid, jasmonates, plant peptide hormones, polyamines, nitricoxide, strigolactones, and triacontanol;

-   -   the microorganisms are comprised of one or more from the group        consisting of bacteria, diazotroph bacteria, diazotrop archaea,        azotobacter vinelandii, clostridium pasteurianu, fungi,        arbuscular mycorrhizal fungi, mycorrhiza, glomus aggrefatum,        glomus etunicatum, glomus intraradices, rhizophagus irregularis,        and glomus mosseae.

TABLE 1 USDA Plants Growth Habit Code: FB; Vigor: 5; Productivity: Good;Flowering timing: 5 weeks to 18 weeks; Flowering score: 7.5; Branches:strong to medium to weak; (a) a cannabidiol content ranging from 0.125weight percent to less than 25 weight percent; (b) atetrahydrocannabinol ranging from 5 weight percent to 63 weight percent;(c) an energy content ranging from between 2,500 British Thermal Unitsper pound to 15,000 British Thermal Units per pound; (d) a carboncontent ranging from between 20 weight percent to 65 weight percent; (e)an oxygen content ranging from between 12 weight percent to 55 weightpercent; (f) a hydrogen content ranging from between 2 weight percent to20 weight percent; (g) an ash content ranging from between 2.5 weightpercent to 30 weight percent; (h) volatiles content ranging from between30 weight percent to 90 weight percent; (i) a nitrogen content rangingfrom between 1 weight percent to 10 weight percent; (j) a sulfur contentranging from between 0.01 weight percent to 8 weight percent; (k) achlorine content ranging from 0.05 weight percent to 5 weight percent;(l) a sodium content ranging from 0.02 weight percent to 15 weightpercent; (m) a potassium content ranging from 0.05 weight percent to 15weight percent; (n) an iron content ranging from 0.01 weight percent to13 weight percent; (o) a magnesium content ranging from 0.02 weightpercent to 10 weight percent; (p) a phosphorous content ranging from0.05 weight percent to 12 weight percent; (q) a calcium content rangingfrom 0.03 weight percent to 10 weight percent; (r) a zinc contentranging from 0.01 weight percent to 5 weight percent; (s) a cellulosecontent ranging from 25 weight percent to 75 weight percent; (t) alignin content ranging from 3 weight percent to 35 weight percent; (u) ahemicellulose content ranging from 3 weight percent to 30 weightpercent; (v) a fat content ranging from 5 weight percent to 35 weightpercent; (w) a fiber content ranging from 5 weight percent to 75 weightpercent; and (x) a protein content ranging from 5 weight percent to 35weight percent; wherein: the Cannabis Sativa L. ssp indica contentranges from 15% to 65%; the Cannabis Sativa L. ssp sativa content rangesfrom 20% to 70%;

In embodiments, DANLEO III has a cannabidiol content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.125 to 0.156, 0.156 to 0.195, 0.195 to0.244, 0.244 to 0.305, 0.305 to 0.381, 0.381 to 0.477, 0.477 to 0.596,0.596 to 0.745, 0.745 to 0.931, 0.931 to 1.164, 1.164 to 1.455, 1.455 to1.819, 1.819 to 2.274, 2.274 to 2.842, 2.842 to 3.553, 3.553 to 4.441,4.441 to 5.551, 5.551 to 6.939, 6.939 to 8.674, 8.674 to 10.842, 10.842to 13.553, 13.553 to 16.941, 16.941 to 21.176, and 21.176 to 25.000.

In embodiments, DANLEO III has a tetrahydrocannabinol content includinga weight percent on a dry basis comprising one or more weight percentsselected from the group consisting of: 5 to 10, 10 to 15, 15 to 20, 20to 25, 25 to 30, 30 to 35, 35 to 40, 40 to 45, 45 to 50, 50 to 55, 55 to60, and 60 to 63.

In embodiments, DANLEO III has an energy content including BritishThermal Units per pound on a dry basis comprising one or more selectedfrom the group consisting of: 2500 to 3000, 3000 to 3500, 3500 to 4000,4000 to 4500, 4500 to 5000, 5000 to 5500, 5500 to 6000, 6000 to 6500,6500 to 7000, 7000 to 7500, 7500 to 8000, 8000 to 8500, 8500 to 9000,9000 to 9500, 9500 to 10000, 10000 to 10500, 10500 to 11000, 11000 to11500, 11500 to 12000, 12000 to 12500, 12500 to 13000, 13000 to 13500,13500 to 14000, 14000 to 14500, and 14500 to 15000.

In embodiments, DANLEO III has a carbon content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 20 to 25, 25 to 30, 30 to 35, 35 to 40, 40to 45, 45 to 50, 50 to 55, 55 to 60, and 60 to 65.

In embodiments, DANLEO III has an oxygen content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 12 to 17, 17 to 22, 22 to 27, 27 to 32, 32to 37, 37 to 42, 42 to 47, 47 to 52, and 52 to 55.

In embodiments, DANLEO III has a hydrogen content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 2 to 4, 4 to 6, 6 to 8, 8 to 10, 10 to 12,12 to 14, 14 to 16, 16 to 18, and 18 to 20.

In embodiments, DANLEO III has an ash content including a weight percenton a dry basis comprising one or more weight percents selected from thegroup consisting of: 2.5 to 5.0, 5.0 to 7.5, 7.5 to 10.0, 10.0 to 12.5,12.5 to 15.0, 15.0 to 17.5, 17.5 to 20.0, 20.0 to 22.5, 22.5 to 25.0,25.0 to 27.5, and 27.5 to 30.0.

In embodiments, DANLEO III has a volatiles content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 30 to 35, 35 to 40, 40 to 45, 45 to 50, 50to 55, 55 to 60, 60 to 65, 65 to 70, 70 to 75, 75 to 80, 80 to 85, and85 to 90.

In embodiments, DANLEO III has a nitrogen content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 1.0 to 1.5, 1.5 to 2.0, 2.0 to 2.5, 2.5 to3.0, 3.0 to 3.5, 3.5 to 4.0, 4.0 to 4.5, 4.5 to 5.0, 5.0 to 5.5, 5.5 to6.0, 6.0 to 6.5, 6.5 to 7.0, 7.0 to 7.5, 7.5 to 8.0, 8.0 to 8.5, 8.5 to9.0, 9.0 to 9.5, and 9.5 to 10.0.

In embodiments, DANLEO III has a sulfur content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.01 to 0.02, 0.02 to 0.04, 0.04 to 0.08,0.08 to 0.16, 0.16 to 0.32, 0.32 to 0.64, 0.64 to 1.28, 1.28 to 1.92,1.92 to 2.88, 2.88 to 4.32, 4.32 to 6.48, and 6.48 to 8.00.

In embodiments, DANLEO III has a chlorine content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.05 to 0.10, 0.10 to 0.20, 0.20 to 0.40,0.40 to 0.80, 0.80 to 1.60, 1.60 to 3.20, 3.20 to 4.80, and 4.80 to5.00.

In embodiments, DANLEO III has a sodium content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.02 to 0.04, 0.04 to 0.08, 0.08 to 0.16,0.16 to 0.32, 0.32 to 0.64, 0.64 to 1.28, 1.28 to 1.92, 1.92 to 2.88,2.88 to 4.32, 4.32 to 6.48, 6.48 to 9.72, 9.72 to 12.15, and 12.15 to15.00.

In embodiments, DANLEO III has a potassium content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.05 to 0.10, 0.10 to 0.20, 0.20 to 0.40,0.40 to 0.80, 0.80 to 1.60, 1.60 to 3.20, 3.20 to 4.80, 4.80 to 6.00,6.00 to 7.50, 7.50 to 9.38, 9.38 to 11.72, 11.72 to 14.65, and 14.65 to15.00.

In embodiments, DANLEO III has an iron content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.01 to 0.02, 0.02 to 0.04, 0.04 to 0.08,0.08 to 0.16, 0.16 to 0.32, 0.32 to 0.64, 0.64 to 0.96, 0.96 to 1.20,1.20 to 1.50, 1.50 to 1.88, 1.88 to 2.34, 2.34 to 2.93, 2.93 to 3.66,3.66 to 4.58, 4.58 to 5.72, 5.72 to 7.15, 7.15 to 8.94, 8.94 to 11.18,and 11.18 to 13.00.

In embodiments, DANLEO III has a magnesium content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.02 to 0.04, 0.04 to 0.08, 0.08 to 0.16,0.16 to 0.32, 0.32 to 0.64, 0.64 to 1.28, 1.28 to 1.92, 1.92 to 2.40,2.40 to 3.00, 3.00 to 3.75, 3.75 to 4.69, 4.69 to 5.86, 5.86 to 7.32,7.32 to 9.16, and 9.16 to 10.00.

In embodiments, DANLEO III has a phosphorous content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.05 to 0.10, 0.10 to 0.20, 0.20 to 0.40,0.40 to 0.80, 0.80 to 1.60, 1.60 to 3.20, 3.20 to 4.80, 4.80 to 6.00,6.00 to 7.50, 7.50 to 9.38, 9.38 to 11.72, and 11.72 to 12.00.

In embodiments, DANLEO III has a calcium content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 0.03 to 0.06, 0.06 to 0.12, 0.12 to 0.24,0.24 to 0.48, 0.48 to 0.96, 0.96 to 1.92, 1.92 to 3.84, 3.84 to 7.68,and 7.68 to 10.00.

In embodiments, DANLEO III has a zinc content including a weight percenton a dry basis comprising one or more weight percents selected from thegroup consisting of: 0.01 to 0.02, 0.02 to 0.04, 0.04 to 0.08, 0.08 to0.16, 0.16 to 0.32, 0.32 to 0.64, 0.64 to 0.80, 0.80 to 1.00, 1.00 to1.25, 1.25 to 1.56, 1.56 to 1.95, 1.95 to 2.44, 2.44 to 3.05, 3.05 to3.81, 3.81 to 4.77, and 4.77 to 5.00.

In embodiments, DANLEO III has a cellulose content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 25 to 30, 30 to 35, 35 to 40, 40 to 45, 45to 50, 50 to 55, 55 to 60, 60 to 65, 65 to 70, and 70 to 75.

In embodiments, DANLEO III has a lignin content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 3 to 6, 6 to 9, 9 to 12, 12 to 15, 15 to18, 18 to 21, 21 to 24, 24 to 27, 27 to 30, 30 to 33, and 33 to 35.

In embodiments, DANLEO III has a hemicellulose content including aweight percent on a dry basis comprising one or more weight percentsselected from the group consisting of: 3 to 6, 6 to 9, 9 to 12, 12 to15, 15 to 18, 18 to 21, 21 to 24, 24 to 27, and 27 to 30.

In embodiments, DANLEO III has a fat content including a weight percenton a dry basis comprising one or more weight percents selected from thegroup consisting of: 5 to 10, 10 to 15, 15 to 20, 20 to 25, 25 to 30,and 30 to 35.

In embodiments, DANLEO III has a fiber content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 5 to 10, 10 to 15, 15 to 20, 20 to 25, 25to 30, 30 to 35, 35 to 40, 40 to 45, 45 to 50, 50 to 55, 55 to 60, 60 to65, 65 to 70, and 70 to 75.

In embodiments, DANLEO III has a protein content including a weightpercent on a dry basis comprising one or more weight percents selectedfrom the group consisting of: 5 to 10, 10 to 15, 15 to 20, 20 to 25, 25to 30, and 30 to 35.

In embodiments, DANLEO III has a Cannabis Sativa L. ssp indica contentranges from: 15 to 20, 20 to 25, 25 to 30, 30 to 35, 35 to 40, 40 to 45,45 to 50, 50 to 55, 55 to 60, or 60 to 65.

In embodiments, DANLEO III has a Cannabis Sativa L. ssp sativa contentranges from: 20 to 25, 25 to 30, 30 to 35, 35 to 40, 40 to 45, 45 to 50,50 to 55, 55 to 60, 60 to 65, or 65 to 70.

In embodiments, the terpenes concentration of DANLEO III cannabis plantincludes on a dry basis: 25 parts per million (ppm) to 50 ppm, 50 ppm to100 ppm, 100 ppm to 200 ppm, 200 ppm to 400 ppm, 400 ppm to 800 ppm, 800ppm to 1600 ppm, 1600 ppm to 3200 ppm, 3200 ppm to 6400 ppm, 6400 ppm to9600 ppm, 9600 ppm to 14400 ppm, 14400 ppm to 21600 ppm, 21600 ppm to32400 ppm, 32400 ppm to 48600 ppm, 48600 ppm to 72900 ppm, 72900 ppm to109350 ppm, 109350 ppm to 164025 ppm, 164025 ppm to 246038 ppm, 246038ppm to 369056 ppm, 369056 ppm to 553584 ppm, and combinations thereof ofvarious different terpenes and terpene concentrations.

In embodiments, the DANLEO III cannabis plant includes a naturalmutation. In embodiments, the DANLEO III cannabis plant includes aninduced mutation. In embodiments, the DANLEO III cannabis plant isdistinguished over the parent plants or related varieties in that ispossesses unique characteristics, including specific ranges of variouscharacteristics and components which make up the plant. In embodiments,the DANLEO III cannabis plant has different levels of chemicalconstituents as compared with the parents as described in the ComparisonTo Parents section of this patent specification. In embodiments, themain differences between the DANLEO III cannabis plant and its parentsare described in the Comparison To Parents section of this patentspecification.

Applicant believes that the description presents a full, clear andcomplete botanical description of the cannabis plant named DANLEO IIIand the characteristics which define the plant and which distinguish theplant from related known cultivars and antecedents. Applicant hascarefully compared the cannabis plant named DANLEO III with thebotanical descriptions set forth in the specification and has ensuredcompleteness and accuracy and to distinguish the plant.

Comparison to Parents:

The parents of DANLEO III were DANLEO I and DANLEO II.

DANLEO I USDA Plants Growth Habit Code: FB; Vigor: 5; Productivity:Good; Flowering timing: 5 weeks to 18 weeks; Flowering score: 7.5;Branches: strong to medium to weak; (a) a cannabidiol content rangingfrom 0.1 weight percent to less than 28 weight percent; (b) atetrahydrocannabinol ranging from 3 weight percent to 65 weight percent;(c) an energy content ranging from between 2,400 British Thermal Unitsper pound to 15,500 British Thermal Units per pound; (d) a carboncontent ranging from between 18 weight percent to 66 weight percent; (e)an oxygen content ranging from between 10 weight percent to 60 weightpercent; (f) a hydrogen content ranging from between 1 weight percent to25 weight percent; (g) an ash content ranging from between 2 weightpercent to 35 weight percent; (h) volatiles content ranging from between25 weight percent to 95 weight percent; (i) a nitrogen content rangingfrom between 0.5 weight percent to 12 weight percent; (j) a sulfurcontent ranging from between 0.005 weight percent to 10 weight percent;(k) a chlorine content ranging from 0.01 weight percent to 7 weightpercent; (l) a sodium content ranging from 0.01 weight percent to 16weight percent; (m) a potassium content ranging from 0.04 weight percentto 16 weight percent; (n) an iron content ranging from 0.008 weightpercent to 15 weight percent; (o) a magnesium content ranging from 0.01weight percent to 12 weight percent; (p) a phosphorous content rangingfrom 0.01 weight percent to 14 weight percent; (q) a calcium contentranging from 0.02 weight percent to 12 weight percent; (r) a zinccontent ranging from 0.005 weight percent to 6 weight percent; (s) acellulose content ranging from 20 weight percent to 78 weight percent;(t) a lignin content ranging from 2 weight percent to 38 weight percent;(u) a hemicellulose content ranging from 2 weight percent to 32 weightpercent; (v) a fat content ranging from 4 weight percent to 38 weightpercent; (w) a fiber content ranging from 4 weight percent to 77 weightpercent; and (x) a protein content ranging from 4 weight percent to 38weight percent; wherein: the Cannabis Sativa L. ssp indica contentranges from 10% to 70%; the Cannabis Sativa L. ssp sativa content rangesfrom 15% to 75%;

DANLEO II USDA Plants Growth Habit Code: FB; Vigor: 5; Productivity:Good; Flowering timing: 5 weeks to 18 weeks; Flowering score: 7.5;Branches: strong to medium to weak; (a) a cannabidiol content rangingfrom 0.15 weight percent to less than 24 weight percent; (b) atetrahydrocannabinol ranging from 8 weight percent to 60 weight percent;(c) an energy content ranging from between 3,000 British Thermal Unitsper pound to 14,500 British Thermal Units per pound; (d) a carboncontent ranging from between 22 weight percent to 60 weight percent; (e)an oxygen content ranging from between 15 weight percent to 50 weightpercent; (f) a hydrogen content ranging from between 3 weight percent to18 weight percent; (g) an ash content ranging from between 3 weightpercent to 28 weight percent; (h) volatiles content ranging from between35 weight percent to 85 weight percent; (i) a nitrogen content rangingfrom between 1.5 weight percent to 9.5 weight percent; (j) a sulfurcontent ranging from between 0.015 weight percent to 7.5 weight percent;(k) a chlorine content ranging from 0.08 weight percent to 4.5 weightpercent; (l) a sodium content ranging from 0.03 weight percent to 14weight percent; (m) a potassium content ranging from 0.06 weight percentto 14 weight percent; (n) an iron content ranging from 0.02 weightpercent to 12 weight percent; (o) a magnesium content ranging from 0.03weight percent to 9 weight percent; (p) a phosphorous content rangingfrom 0.06 weight percent to 11 weight percent; (q) a calcium contentranging from 0.04 weight percent to 9 weight percent; (r) a zinc contentranging from 0.02 weight percent to 4.5 weight percent; (s) a cellulosecontent ranging from 26 weight percent to 70 weight percent; (t) alignin content ranging from 4 weight percent to 33 weight percent; (u) ahemicellulose content ranging from 4 weight percent to 28 weightpercent; (v) a fat content ranging from 6 weight percent to 33 weightpercent; (w) a fiber content ranging from 6 weight percent to 70 weightpercent; and (x) a protein content ranging from 6 weight percent to 33weight percent; wherein: the Cannabis Sativa L. ssp indica contentranges from 20% to 60%; the Cannabis Sativa L. ssp sativa content rangesfrom 25% to 65%;FIG. 23′

FIG. 23′ shows one non-limiting embodiment of a cannabis cloningassembly (CA). In embodiments, the cannabis cloning assembly (CA)includes a plurality of containers (TY1, TY2, TY3, TY^(N), TY^(N+1))connected to at least one cloning enclosure (CHD). The cloning enclosure(CHD) when placed upon the plurality of containers (TY1, TY2, TY3,TY^(N), TY^(N+1)) forms an interior (CHD-1). In embodiments, the cloningenclosure (CHD) does not let humidity, water vapor, carbon dioxide, orair to escape from within the interior (CHD-1). The cloning enclosure(CHD) is configured to contain humidity in the interior (CHD-1) abovethe plurality of containers (TY1, TY2, TY3, TY^(N), TY^(N+1)). Inembodiments, insects are grown within the cannabis cloning assembly(CA). In embodiments, the cannabis plants are cloned using aeroponicmethodologies as described in detail above.

The cannabis cloning assembly (CA) is configured to asexually reproduceDANLEO III (107, 207) that grow within in each growing assembly (100,200). The present disclosure provides for a method to asexually clone aplurality of DANLEO III (107, 207) plants, the method includes:

-   -   (a) providing:        -   (a0) a plurality of DANLEO III (107, 207) plants;        -   (a1) a cutting tool (CT1);        -   (a2) a liquid, powder, or gel rooting solution (RS), the            rooting solution includes one or more from the group            consisting of water, carbohydrates, enzymes, vitamins,            hormones, and microorganisms;        -   (a3) a growing medium (GM), the growing medium includes one            or more from the group consisting of rockwool, perlite,            amorphous volcanic glass, vermiculite, clay, clay pellets,            LECA (lightweight expanded clay aggregate), coco-coir,            fibrous coconut husks, soil, dirt, peat, peat moss, sand,            soil, compost, manure, fir bark, foam, gel, oasis cubes,            lime, gypsum, quartz, plastic, polyethylene, high-density            polyethylene (HDPE), low-density polyethylene (LDPE),            polyethylene terephthalate (PET), polyacrylonitrile, and            polypropylene;        -   (a4) a plurality of containers (TY1, TY2, TY3, TY^(N),            TY^(N+1)) configured to accept the rooting solution (RS) and            the growing medium (GM), the plurality of containers are            configured to be positioned within a cloning enclosure            (CHD);        -   (a5) the cloning enclosure (CHD) has an interior (CHD-1),            the cloning enclosure (CHD) is configured to contain water            vapor within the interior (CHD-1) to provide a humid            environment for plants within the interior (CHD-1);    -   (b) introducing the rooting solution and the growing medium to        the plurality of containers;    -   (c) using the cutting tool to sever the tips from a plurality of        Cannabis plants to form a plurality of severed plants (107X,        207X);    -   (d) inserting the plurality of severed plants (107X, 207X) of        step (c) into the plurality of containers;    -   (e) placing the plurality of containers within the interior of        the cloning enclosure;    -   (f) illuminating the plants after step (e);    -   (g) growing the plants until roots are formed; and    -   (h) optionally venting the interior of the cloning enclosure;

wherein:

the carbohydrates are comprised of one or more from the group consistingof sugar, sucrose, molasses, and plant syrups;

the enzymes are comprised of one or more from the group consisting ofamino acids, orotidine 5′-phosphate decarboxylase, OMP decarboxylase,glucanase, beta-glucanase, cellulase, xylanase, HYGROZYME®, CANNAZYME®,MICROZYME®, and SENSIZYME®;

the vitamins are comprised of one or more from the group consisting ofvitamin B, vitamin C, vitamin D, and vitamin E;

the hormones are comprised of one or more from the group consisting ofauxins, cytokinins gibberellins, abscic acid, brassinosteroids,salicylic acid, jasmonates, plant peptide hormones, polyamines, nitricoxide, strigolactones, and triacontanol;

the microorganisms are comprised of one or more from the groupconsisting of bacteria, diazotroph bacteria, diazotrop archaea,azotobacter vinelandii, clostridium pasteurianu, fungi, arbuscularmycorrhizal fungi, mycorrhiza, glomus aggrefatum, glomus etunicatum,glomus intraradices, rhizophagus irregularis, and glomus mosseae.

The cannabis cloning assembly (CA) is configured to asexually reproduceDANLEO III (107, 207) that grow within in each growing assembly (100,200). The present disclosure provides for a method to asexually clone aplurality of DANLEO III (107, 207) plants, the method includes:

-   -   (a) providing:        -   (a0) a plurality of DANLEO III (107, 207) plants;        -   (a1) a cutting tool (CT1);        -   (a2) a liquid, powder, or gel rooting solution (RS), the            rooting solution includes one or more from the group            consisting of water, carbohydrates, enzymes, vitamins,            hormones, and microorganisms;        -   (a3) a growing medium (GM), the growing medium includes a            gel;        -   (a4) a plurality of containers (TY1, TY2, TY3, TY^(N),            TY^(N+1)) configured to accept the rooting solution (RS) and            the growing medium (GM), the plurality of containers are            configured to be positioned within a cloning enclosure            (CHD);        -   (a5) the cloning enclosure (CHD) has an interior (CHD-1),            the cloning enclosure (CHD) is configured to contain water            vapor within the interior (CHD-1) to provide a humid            environment for plants within the interior (CHD-1);    -   (b) introducing the rooting solution and the growing medium to        the plurality of containers;    -   (c) using the cutting tool to sever the tips from a plurality of        Cannabis plants to form a plurality of severed plants (107X,        207X), and blending the tips into a slurry comprising water, and        mixing the slurry with the rooting solution (RS) and the growing        medium    -   (GM);    -   (d) introducing the slurry of step (c) into the plurality of        containers;    -   (e) placing the plurality of containers within the interior of        the cloning enclosure;    -   (f) illuminating the slurry after step (e);    -   (g) growing the slurry until roots are formed; and    -   (h) optionally venting the interior of the cloning enclosure;

wherein:

the carbohydrates are comprised of one or more from the group consistingof sugar, sucrose, molasses, and plant syrups;

the enzymes are comprised of one or more from the group consisting ofamino acids, orotidine 5′-phosphate decarboxylase, OMP decarboxylase,glucanase, beta-glucanase, cellulase, xylanase, HYGROZYME®, CANNAZYME®,MICROZYME®, and SENSIZYME®;

the vitamins are comprised of one or more from the group consisting ofvitamin B, vitamin C, vitamin D, and vitamin E;

the hormones are comprised of one or more from the group consisting ofauxins, cytokinins gibberellins, abscic acid, brassinosteroids,salicylic acid, jasmonates, plant peptide hormones, polyamines, nitricoxide, strigolactones, and triacontanol;

the microorganisms are comprised of one or more from the groupconsisting of bacteria, diazotroph bacteria, diazotrop archaea,azotobacter vinelandii, clostridium pasteurianu, fungi, arbuscularmycorrhizal fungi, mycorrhiza, glomus aggrefatum, glomus etunicatum,glomus intraradices, rhizophagus irregularis, and glomus mosseae.

Thus, specific systems and methods of an Insect ProductionSuperstructure System (IPSS) and/or a Farming Superstructure System(IPSS) have been disclosed. It should be apparent, however, to thoseskilled in the art that many more modifications besides those alreadydescribed are possible without departing from the inventive conceptsherein. The inventive subject matter, therefore, is not to be restrictedexcept in the spirit of the disclosure.

Thus, the applicant(s) should be understood to have support to claim andmake a statement of invention to at least: i) each of the processdevices as herein disclosed and described, ii) the related methodsdisclosed and described, iii) similar, equivalent, and even implicitvariations of each of these devices and methods, iv) those alternativedesigns which accomplish each of the functions shown as are disclosedand described, v) those alternative designs and methods which accomplisheach of the functions shown as are implicit to accomplish that which isdisclosed and described, vi) each feature, component, and step shown asseparate and independent inventions, vii) the applications enhanced bythe various systems or components disclosed, viii) the resultingproducts produced by such systems or components, ix) each system,method, and element shown or described as now applied to any specificfield or devices mentioned, x) methods and apparatuses substantially asdescribed hereinbefore and with reference to any of the accompanyingexamples, xi) the various combinations and permutations of each of theelements disclosed, xii) each potentially dependent claim or concept asa dependency on each and every one of the independent claims or conceptspresented, and xiii) all inventions described herein.

With regard to claims whether now or later presented for examination, itshould be understood that for practical reasons and so as to avoid greatexpansion of the examination burden, the applicant may at any timepresent only initial claims or perhaps only initial claims with onlyinitial dependencies. Support should be understood to exist to thedegree required under new matter laws—including but not limited toEuropean Patent Convention Article 123(2) and United States Patent Law35 USC 132 or other such laws—to permit the addition of any of thevarious dependencies or other elements presented under one independentclaim or concept as dependencies or elements under any other independentclaim or concept. In drafting any claims at any time whether in thisapplication or in any subsequent application, it should also beunderstood that the applicant has intended to capture as full and broada scope of coverage as legally available. To the extent thatinsubstantial substitutes are made, to the extent that the applicant didnot in fact draft any claim so as to literally encompass any particularembodiment, and to the extent otherwise applicable, the applicant shouldnot be understood to have in any way intended to or actuallyrelinquished such coverage as the applicant simply may not have beenable to anticipate all eventualities; one skilled in the art, should notbe reasonably expected to have drafted a claim that would have literallyencompassed such alternative embodiments.

Further, if or when used, the use of the transitional phrase“comprising” is used to maintain the “open-end” claims herein, accordingto traditional claim interpretation. Thus, unless the context requiresotherwise, it should be understood that the term “comprise” orvariations such as “comprises” or “comprising”, are intended to implythe inclusion of a stated element or step or group of elements or stepsbut not the exclusion of any other element or step or group of elementsor steps. Such terms should be interpreted in their most expansive formso as to afford the applicant the broadest coverage legally permissible.

Finally, any claims set forth at any time are hereby incorporated byreference as part of this description of the inventive technology, andthe applicant expressly reserves the right to use all of or a portion ofsuch incorporated content of such claims as additional description tosupport any of or all of the claims or any element or component thereof,and the applicant further expressly reserves the right to move anyportion of or all of the incorporated content of such claims or anyelement or component thereof from the description into the claims orvice-versa as necessary to define the matter for which protection issought by this application or by any subsequent continuation, division,or continuation-in-part application thereof, or to obtain any benefitof, reduction in fees pursuant to, or to comply with the patent laws,rules, or regulations of any country or treaty, and such contentincorporated by reference shall survive during the entire pendency ofthis application including any subsequent continuation, division, orcontinuation-in-part application thereof or any reissue or extensionthereon.

Although the foregoing text sets forth a detailed description ofnumerous different embodiments of the disclosure, it should beunderstood that the scope of the disclosure is defined by the words ofthe claims set forth at the end of this patent. The detailed descriptionis to be construed as exemplary only and does not describe everypossible embodiment of the disclosure because describing every possibleembodiment would be impractical, if not impossible. Numerous alternativeembodiments could be implemented, using either current technology ortechnology developed after the filing date of this patent, which wouldstill fall within the scope of the claims defining the disclosure.

Thus, many modifications and variations may be made in the techniquesand structures described and illustrated herein without departing fromthe spirit and scope of the present disclosure. Accordingly, it shouldbe understood that the methods and apparatus described herein areillustrative only and are not limiting upon the scope of the disclosure.

Unless the context dictates the contrary, all ranges set forth hereinshould be interpreted as being inclusive of their endpoints, andopen-ended ranges should be interpreted to include commerciallypractical values. Similarly, all lists of values should be considered asinclusive of intermediate values unless the context indicates thecontrary.

The recitation of ranges of values herein is merely intended to serve asa shorthand method of referring individually to each separate valuefalling within the range. Unless otherwise indicated herein, eachindividual value is incorporated into the specification as if it wereindividually recited herein. All methods described herein can beperformed in any suitable order unless otherwise indicated herein orotherwise clearly contradicted by context. The use of any and allexamples, or exemplary language (e.g., “such as”) provided with respectto certain embodiments herein is intended merely to better illuminatethe disclosure and does not pose a limitation on the scope of thedisclosure otherwise claimed. No language in the specification should beconstrued as indicating any non-claimed element essential to thepractice of the disclosure.

Groupings of alternative elements or embodiments of the disclosuredisclosed herein are not to be construed as limitations. Each groupmember can be referred to and claimed individually or in any combinationwith other members of the group or other elements found herein. One ormore members of a group can be included in, or deleted from, a group forreasons of convenience and/or patentability. When any such inclusion ordeletion occurs, the specification is herein deemed to contain the groupas modified thus fulfilling the written description of all Markushgroups used in the appended claims.

It should be apparent to those skilled in the art that many moremodifications besides those already described are possible withoutdeparting from the inventive concepts herein. The inventive subjectmatter, therefore, is not to be restricted except in the spirit of theappended claims. Moreover, in interpreting both the specification andthe claims, all terms should be interpreted in the broadest possiblemanner consistent with the context. In particular, the terms “comprises”and “comprising” should be interpreted as referring to elements,components, or steps in a non-exclusive manner, indicating that thereferenced elements, components, or steps may be present, or utilized,or combined with other elements, components, or steps that are notexpressly referenced. Where the specification claims refer to at leastone of something selected from the group consisting of A, B, C . . . andN, the text should be interpreted as requiring only one element from thegroup, not A plus N, or B plus N, etc.

Unless defined otherwise, all technical and scientific terms used hereinhave the same meaning as commonly understood by one of ordinary skill inthe art to which this invention belongs. Although any methods andmaterials similar or equivalent to those described herein can also beused in the practice or testing of the present invention, a limitednumber of the exemplary methods and materials are described herein. Itmust be noted that as used herein and in the appended claims, thesingular forms “a”, “an”, and “the” include plural referents unless thecontext clearly dictates otherwise.

The invention claimed is:
 1. A distilled composition comprising amixture of: a biosynthetic cannabinoid derived from a geneticallymodified microorganism; and a non-biosynthetic cannabinoid derived fromcannabis plants.
 2. The composition according to claim 1, wherein: thegenetically modified microorganism comprises genetically modifiedphotosynthetic microalgae.
 3. The composition according to claim 1,wherein: the genetically modified microorganism comprises geneticallymodified bacteria.
 4. The composition according to claim 3, wherein: thegenetically modified bacteria comprise genetically modifiedcyanobacterium.
 5. The composition according to claim 1, comprising: aterpene derived from cannabis plants.
 6. The composition according toclaim 1, comprising: a terpene derived from a genetically engineeredmicroorganism.
 7. The composition according to claim 1, wherein: thecomposition comprises a liquid.
 8. The composition according to claim 1,wherein said cannabinoid is selected from the group consisting oftetrahydrocannabinolic acid, active tetrahydrocannabinol,tetrahydrocannabinol, Δ9-tetrahydrocannabinol, Δ8-tetrahydrocannabinol,cannabichromene, cannabidiol, cannabigerol, cannabinidiol, andcannabinol.
 9. The composition according to claim 1, wherein saidgenetically modified microorganism is derived from a cloned geneticallymodified microorganism.
 10. The composition according to claim 9,wherein said cloned genetically modified microorganism is derived from acloned genetically modified gas fermenting microorganism that hasundergone anaerobic respiration.
 11. The composition according to claim9, wherein said cloned genetically modified organism is selected fromthe group consisting of polyclonal genetically modified microorganism,an oligoclonal genetically modified microorganism, and a monoclonalgenetically modified microorganism.
 12. The composition according toclaim 1, further comprising psilocybin.
 13. A method to produce acannabinoid product from a distilled composition comprising a mixture ofa biosynthetic cannabinoid derived from a genetically modifiedmicroorganism and a non-biosynthetic cannabinoid derived from cannabisplants, the method comprises: (i) emulsifying the distilled compositionin water to produce an emulsion, the emulsion comprises the cannabinoidproduct; or (ii) spray drying a liquid mixture comprising the distilledcomposition to produce a powder, wherein the distilled composition issolubilized in a liquid to produce the liquid mixture and then spraydrying the liquid mixture to produce the powder, the powder comprisesthe cannabinoid product; or (iii) crystallizing the distilledcomposition to produce a crystal, wherein the distilled composition iscrystallized with a device selected from the group consisting of acrystallizer, a draft tube and baffle crystallizer, coolingcrystallization, evaporative crystallization, and fractionalcrystallization, the crystal comprises the cannabinoid product.
 14. Amethod to produce a foodstuff from a distilled composition comprising amixture of a biosynthetic cannabinoid derived from a geneticallymodified microorganism and a non-biosynthetic cannabinoid derived fromcannabis plants, the method comprises: (i) providing the distilledmixture of a biosynthetic cannabinoid derived from a geneticallymodified microorganism and a non-biosynthetic cannabinoid derived fromcannabis plants; and (ii) producing the foodstuff by mixing thefoodstuff with said distilled mixture of step (i), wherein the foodstuffis selected from the group consisting of ada, bagels, baked goods,beverages, biscuits, bitterballen, bonda, breads, cakes, candies,cereals, chips, chocolate bars, carbonated soft drinks, carbonateddrinks, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crepes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, pofferties, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,soft drinks, sport drinks, sparkling drinks, specialty milk, tele-bhaja, tempura, toffee, tortillas, totopo, turkish delights, and waffles.15. A cannabinoid nanoemulsion beverage, comprising: a distilledbiosynthetic cannabinoid derived from a genetically modifiedmicroorganism or a distilled non-biosynthetic cannabinoid derived fromcannabis plants; treated water, wherein the treated water is derivedfrom a water treatment process selected from the group consisting ofcation exchange, anion exchange, membrane filtration, and adsorbentfiltration; and one or more emulsifiers selected from the groupconsisting of a surfactant, a nonionic surfactant, lecithin,polyethylene(40), stearate, polysorbate, polyoxyethylene sorbitanmonoleate, polyoxyethylene(20) sorbitan monoleate, polysorbate 80,polysorbate 60, polysorbate 65, ammonium salts of phosphatidic acid,sucrose acetate isobutyrate, potassium pyrophosphate, sodium acidpyrophosphate, sodium pyrophosphate, potassium polymetaphosphate, sodiummetaphosphate, insoluble or sodium polyphosphates, sodiumpolyphosphates, insoluble polyphosphates, glassy salts of fatty acids,mono- and di-glycerides of fatty acids, mono-glycerides of fatty acids,di-glycerides of fatty acids, acetic and fatty acid esters of glycerol,lactic and fatty acid esters of glycerol, citric and fatty acid estersof glycerol, diacetyltartaric and fatty acid esters of glycerol, mixedfatty acid esters of glycerol, sucrose esters of fatty acids,polyglycerol esters of fatty acids, polyglycerol esters ofinteresterified ricinoleic acid, propylene glycol mono- and di-esters,propylene glycol di-esters, propylene glycol mono-esters, propyleneglycol esters of fatty acids, propylene glycol esters, dioctyl sodiumsulphosuccinate, sodium lactylate, sodium oleyl lactylate, sodiumstearoyl lactylate, calcium lactylate, calcium oleyl lactylate, calciumstearoyl lactylate, sorbitan monostearate, maltodextrin, polyphosphates,formulated polyphosphates, and gum arabic; wherein said cannabinoidnanoemulsion beverage includes: a cannabinoid droplet size ranging from10 to 100 nanometers, a serving size ranging from 6 to 16 fluid ounces,a calorie content ranging from 0 to 200 calories per serving, and acannabinoid content ranging from 2 to 60 milligrams per serving.
 16. Thecannabinoid nanoemulsion beverage according to claim 15, furthercomprising one or more acids, wherein said acid is selected from thegroup consisting of acetic acid, ascorbic acid, benzoic acid, citricacid, formic acid, fumaric acid, hydrochloric acid, lactic acid, malicacid, nitric acid, phosphoric acid, propionic acid, salicylic acid,sulfamic acid, sulfuric acid, and tartaric acid.
 17. The cannabinoidnanoemulsion beverage according to claim 15, further comprising one ormore oils, wherein said oil is selected from the group consisting ofalmond oil, an animal-based oil, apricot kernel oil, avocado oil, brazilnut oil, butter, canola oil, cashew oil, cocoa butter, coconut oil, cornoil, cottonseed oil, fish oil, grapeseed oil, hazelnut oil, insect oil,lard, lard oil, macadamia nut oil, mustard oil, olive oil, palm kerneloil, palm oil, peanut oil, rapeseed oil, rice oil, rice bran oil,safflower oil, semi-refined sesame oil, semi-refined sunflower oil,sesame oil, soybean oil, tallow of beef, tallow of mutton, vegetableoil, and walnut oil.
 18. The cannabinoid nanoemulsion beverage accordingto claim 15, further comprising one or more sweeteners, wherein saidsweetener is selected from the group consisting of aspartame, acesulfamepotassium, saccharin, sucralose, neotame, erythritol, stevia, stevialeaf extract, a sugar alcohol, and a polyol.
 19. A carbonatedcannabinoid nanoemulsion beverage comprising: water; a distilledbiosynthetic cannabinoid derived from a genetically modifiedmicroorganism or a distilled non-biosynthetic cannabinoid derived fromcannabis plants; wherein said carbonated cannabinoid nanoemulsionbeverage comprises: a cannabinoid droplet size ranging from 10 to 100nanometers, a serving size ranging from 6 to 16 fluid ounces, a caloriecontent ranging from 0 to 200 calories per serving, and a cannabinoidcontent ranging from 2 to 60 milligrams per serving; wherein saidcarbonated cannabinoid nanoemulsion beverage further comprises one ormore acids, wherein said acid is selected from the group consisting ofacetic acid, ascorbic acid, benzoic acid, citric acid, folic acid,formic acid, fumaric acid, hydrochloric acid, lactic acid, malic acid,nitric acid, phosphoric acid, propionic acid, salicylic acid, sulfamicacid, sulfuric acid, and tartaric acid.
 20. The carbonated cannabinoidnanoemulsion beverage according to claim 19, wherein said water isderived from one or more water treatment processes wherein said watertreatment process is selected from the group of cation exchange, anionexchange, membrane filtration, and adsorbent filtration.
 21. Thecarbonated cannabinoid nanoemulsion beverage according to claim 19,further comprising one or more oils, wherein said oil is selected fromthe group consisting of almond oil, an animal-based oil, apricot kerneloil, avocado oil, brazil nut oil, butter, canola oil, cashew oil, cocoabutter, coconut oil, corn oil, cottonseed oil, fish oil, grapeseed oil,hazelnut oil, insect oil, lard, lard oil, macadamia nut oil, mustardoil, olive oil, palm kernel oil, palm oil, peanut oil, rapeseed oil,rice oil, rice bran oil, safflower oil, semi-refined sesame oil,semi-refined sunflower oil, sesame oil, soybean oil, tallow of beef,tallow of mutton, vegetable oil, and walnut oil.
 22. The carbonatedcannabinoid nanoemulsion beverage according to claim 19, furthercomprising one or more biocatalyst, wherein said biocatalyst is selectedfrom the group consisting of yeast, bacteria, and a fungus.
 23. Acannabinoid nanoemulsion beverage, comprising water and a distilledbiosynthetic cannabinoid derived from a genetically modifiedmicroorganism or a distilled non-biosynthetic cannabinoid derived fromcannabis plants; wherein said cannabinoid nanoemulsion beveragecomprises: a cannabinoid droplet size ranging from between 10 to 100nanometers, a serving size ranging from 6 to 16 fluid ounces, a caloriecontent ranging from 0 to 200 calories per serving, and a cannabinoidcontent ranging from 2 to 60 milligrams per serving; wherein saidcannabinoid nanoemulsion beverage further comprises one or moresweeteners, wherein said sweetener is selected from the group consistingof aspartame, acesulfame potassium, saccharin, sucralose, neotame,erythritol, stevia, stevia leaf extract, a sugar alcohol, and a polyol.24. The cannabinoid nanoemulsion beverage according to claim 23, whereinsaid water is derived from one or more water treatment processes whereinsaid water treatment process is selected from the group of cationexchange, anion exchange, membrane filtration, and adsorbent filtration.25. The cannabinoid nanoemulsion beverage according to claim 23, furthercomprising one or more acids, wherein said acid is selected from thegroup consisting of acetic acid, ascorbic acid, benzoic acid, citricacid, folic acid, formic acid, fumaric acid, hydrochloric acid, lacticacid, malic acid, nitric acid, phosphoric acid, propionic acid,salicylic acid, sulfamic acid, sulfuric acid, and tartaric acid.
 26. Thecannabinoid nanoemulsion beverage according to claim 23, furthercomprising one or more oils, wherein said oil is selected from the groupconsisting of almond oil, an animal-based oil, apricot kernel oil,avocado oil, brazil nut oil, butter, canola oil, cashew oil, cocoabutter, coconut oil, corn oil, cottonseed oil, fish oil, grapeseed oil,hazelnut oil, insect oil, lard, lard oil, macadamia nut oil, mustardoil, olive oil, palm kernel oil, palm oil, peanut oil, rapeseed oil,rice oil, rice bran oil, safflower oil, semi-refined sesame oil,semi-refined sunflower oil, sesame oil, soybean oil, tallow of beef,tallow of mutton, vegetable oil, and walnut oil.
 27. A compositioncomprising a mixture of: a distilled biosynthetic cannabinoid derivedfrom a genetically modified microorganism; and a distillednon-biosynthetic cannabinoid derived from cannabis plants.
 28. Acannabinoid crystal product derived from a distilled compositioncomprising a biosynthetic cannabinoid derived from a geneticallymodified microorganism or a non-biosynthetic cannabinoid derived fromcannabis plants, wherein the distilled composition is crystallized inone or more crystallizers selected from the group consisting of a drafttube and baffle crystallizer, cooling crystallization, evaporativecrystallization, and fractional crystallization, to produce thecannabinoid crystal product.
 29. The cannabinoid crystal productaccording to claim 28, wherein the purity of the biosyntheticcannabinoid derived from a genetically modified microorganism or thenon-biosynthetic cannabinoid derived from cannabis plants ranges frombetween 95 to 99.75 percent.
 30. The cannabinoid crystal productaccording to claim 29, wherein said biosynthetic cannabinoid derivedfrom a genetically modified microorganism or said non-biosyntheticcannabinoid derived from cannabis plants is selected from the groupconsisting of tetrahydrocannabinolic acid, active tetrahydrocannabinol,tetrahydrocannabinol, Δ9-tetrahydrocannabinol, Δ8-tetrahydrocannabinol,cannabichromene, cannabinidiol, and cannabinol.
 31. The cannabinoidcrystal product according to claim 29, wherein said biosyntheticcannabinoid derived from a genetically modified microorganism or saidnon-biosynthetic cannabinoid derived from cannabis plants comprisescannabidiol.
 32. The cannabinoid crystal product according to claim 29,wherein said biosynthetic cannabinoid derived from a geneticallymodified microorganism or said non-biosynthetic cannabinoid derived fromcannabis plants comprises cannabigerol.
 33. The cannabinoid crystalproduct according to claim 29, wherein said biosynthetic cannabinoidderived from a genetically modified microorganism or saidnon-biosynthetic cannabinoid derived from cannabis plants comprises amolecular weight of about 314.47 grams per mole.
 34. The cannabinoidcrystal product according to claim 28, further comprising pectin. 35.The cannabinoid crystal product according to claim 28, furthercomprising pentane.
 36. The composition according to claim 28, furthercomprising one or more waxes, wherein said wax is selected from thegroup consisting of mimosa flower wax, almond wax, avocado wax, beerywax, bees wax, ylang ylang flower wax, candelilla wax, castor wax,cupuacu butter, hemp wax, jasmine flower wax, lavender flower wax,mmyrica fruit wax, olive wax, rapeseed wax, rice bran wax, rose flowerwax, shea butter, soybean wax, sunflower wax, vegan wax, vegetable wax,wax from Mexican shrub Euphorbia antisyphilitica, and wax from theberries of rhus verniciflua.
 37. The composition according to claim 28,further comprising one or more solubilizing agents, wherein saidsolubilizing agent is selected from the group consisting of acacia,cholesterol, diethanolamine, glyceryl monostearate, lanolin alcohols,mono- and di-glycerides, monoethanolamine, lecithin, oleyl alcohol,poloxamer, polyoxyethylene 50 stearate, polyoxyl 35 castor oil, polyoxyl40 hydrogenated castor oil, polyoxyl 10 oleyl ether, polyoxyl 20cetostearyl ether, polyoxyl 40 stearate, polysorbate 20, polysorbate 40,polysorbate 60, polysorbate 80, sodium lauryl sulfate, sodium stearate,sorbitan monolaurate, sorbitan monooleate, sorbitan monopalmitate,sorbitan monostearate, and trolamine.
 38. The composition according toclaim 28, further comprising one or more oils, wherein said oil isselected from the group consisting of almond oil, an animal-based oil,apricot kernel oil, avocado oil, brazil nut oil, butter, canola oil,cashew oil, cocoa butter, coconut oil, corn oil, cottonseed oil, fishoil, grapeseed oil, hazelnut oil, insect oil, lard, lard oil, macadamianut oil, mustard oil, olive oil, palm kernel oil, palm oil, peanut oil,rapeseed oil, rice oil, rice bran oil, safflower oil, semi-refinedsesame oil, semi-refined sunflower oil, sesame oil, soybean oil, tallowof beef, tallow of mutton, vegetable oil, and walnut oil.
 39. Thecomposition according to claim 28, further comprising water, whereinsaid water is derived from one or more water treatment processes whereinsaid water treatment process is selected from the group of cationexchange, anion exchange, membrane filtration, and adsorbent filtration.40. The composition according to claim 28, further comprising one ormore acids, wherein said acid is selected from the group consisting ofacetic acid, ascorbic acid, benzoic acid, citric acid, dehydroaceticacid, formic acid, fumaric acid, hydrochloric acid, lactic acid, malicacid, nitric acid, oleic acid, phosphoric acid, propionic acid,salicylic acid, sorbic acid, sulfamic acid, sulfuric acid, stearic acid,and tartaric acid.
 41. The composition according to claim 28, furthercomprising one or more perfumes, wherein said perfume is selected fromthe group consisting of anethole, benzaldehyde, ethyl vanillin, menthol,methyl salicylate, orange flower oil, peppermint, peppermint oil,peppermint spirit, rose oil, thymol, tolu balsam tincture, vanilla, andvanillin.
 42. A spray-dried cannabinoid powder product derived from adistilled composition comprising a biosynthetic cannabinoid derived froma genetically modified microorganism or a non-biosynthetic cannabinoidderived from cannabis plants, said spray-dried cannabinoid powdercomprises a particle size ranging from between 100 nanometers to 10microns and is produced in one or more types of spray-dryers selectedfrom the group consisting of a co-current type spray dryer, acounter-current type spray dryer, and a mixed-flow type spray dryer. 43.The spray-dried cannabinoid powder product according to claim 42,wherein the purity of the biosynthetic cannabinoid derived from agenetically modified microorganism or the non-biosynthetic cannabinoidderived from cannabis plants ranges from between 95 to 99.75 percent.44. The spray-dried cannabinoid powder product according to claim 43,wherein said biosynthetic cannabinoid derived from a geneticallymodified microorganism or said non-biosynthetic cannabinoid derived fromcannabis plants is selected from the group consisting oftetrahydrocannabinolic acid, active tetrahydrocannabinol,tetrahydrocannabinol, Δ9-tetrahydrocannabinol, Δ8-tetrahydrocannabinol,cannabichromene, cannabinidiol, cannabidiol, cannabigerol, andcannabinol.
 45. The spray-dried cannabinoid powder product according toclaim 43, wherein said biosynthetic cannabinoid derived from agenetically modified microorganism or said non-biosynthetic cannabinoidderived from cannabis plants comprises a molecular weight of about314.47 grams per mole.
 46. An animal food cannabinoid product derivedfrom a distilled composition comprising a biosynthetic cannabinoidderived from a genetically modified microorganism or a non-biosyntheticcannabinoid derived from cannabis plants.
 47. The animal foodcannabinoid product according to claim 46, wherein the biosyntheticcannabinoid derived from a genetically modified microorganism or thenon-biosynthetic cannabinoid derived from cannabis plants is selectedfrom the group consisting of powder and a crystal.
 48. A foodstuffcomprising a distilled composition comprising a biosynthetic cannabinoidderived from a genetically modified microorganism or a non-biosyntheticcannabinoid derived from cannabis plants, wherein the foodstuff isselected from the group consisting of ada, bagels, baked goods,beverages, biscuits, bitterballen, bonda, breads, cakes, candies,cereals, chips, chocolate bars, carbonated soft drinks, carbonateddrinks, chocolate, coffee, cokodok, confectionery, cookies, cookingbatter, corn starch mixtures, crackers, crepes, croissants, croquettes,croutons, dolma, dough, doughnuts, energy bars, flapjacks, french fries,frozen custard, frozen desserts, frying cakes, fudge, gelatin mixes,granola bars, gulha, hardtack, ice cream, khandvi, khanom buang,krumpets, meze, mixed flours, muffins, multi-grain snacks, nachos, niangao, noodles, nougat, onion rings, pakora, pancakes, panforte, pastas,pastries, pie crust, pita chips, pizza, pofferties, pretzels, proteinpowders, pudding, rice krispie treats, sesame sticks, smoothies, snacks,soft drinks, sport drinks, sparkling drinks, specialty milk, tele-bhaja,tempura, toffee, tortillas, totopo, turkish delights, and waffles. 49.The foodstuff according to claim 48, wherein the biosyntheticcannabinoid derived from a genetically modified microorganism or thenon-biosynthetic cannabinoid derived from cannabis plants is selectedfrom the group consisting of powder and a crystal.
 50. A cooked foodcomposition, wherein the composition is cooked in one or more selectedfrom the group consisting of an oven, a dryer, a dehydrator, and afreeze dryer, the composition includes: a mixture comprising water, adistilled biosynthetic cannabinoid derived from a genetically modifiedmicroorganism or a distilled non-biosynthetic cannabinoid derived fromcannabis plants, and two or more ingredients selected from the groupconsisting of insects, a binding agent, and an acid; wherein: saidinsects are selected from the group consisting of an insect lipid,Orthoptera order of insects, crickets, katydids, weta, lubber, acrida,locusts, cicadas, Hermetia illucens, beetles, mealworms, yellow mealwormbeetles, and Tenebrio molitor; said binding agent is selected from thegroup consisting of agar, agave, alginin, arrowroot, carrageenan,collagen, cornstarch, egg whites, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, protein,psyllium husks, sago, sugar, syrup, tapioca, vegetable gum, and xanthangum; said acid is selected from the group consisting of acetic acid,ascorbic acid, benzoic acid, citric acid, formic acid, fumaric acid,hydrochloric acid, lactic acid, malic acid, nitric acid, phosphoricacid, propionic acid, salicylic acid, sulfuric acid, and tartaric acid.51. The composition according to claim 50, further comprising a bindingagent mass ratio ranging from between 10 to 750 pounds of the bindingagent per ton of the composition.
 52. The composition according to claim50, wherein the biosynthetic cannabinoid derived from a geneticallymodified microorganism or the non-biosynthetic cannabinoid derived fromcannabis plants is selected from the group consisting of powder and acrystal.
 53. The composition according to claim 50, further comprisingone or more oils, wherein said oil is selected from the group consistingof almond oil, an animal-based oil, apricot kernel oil, avocado oil,brazil nut oil, butter, canola oil, cashew oil, cocoa butter, coconutoil, corn oil, cottonseed oil, fish oil, grapeseed oil, hazelnut oil,insect oil, lard, lard oil, macadamia nut oil, mustard oil, olive oil,palm kernel oil, palm oil, peanut oil, rapeseed oil, rice oil, rice branoil, safflower oil, semi-refined sesame oil, semi-refined sunflower oil,sesame oil, soybean oil, tallow of beef, tallow of mutton, vegetableoil, and walnut oil.
 54. The composition according to claim 50, furthercomprising one or more selected from the group consisting of afiber-starch material, a density improving textural supplement, and amoisture improving textural supplement; wherein: said fiber-starchmaterial is selected from the group consisting of a cereal-grain-basedmaterial, a grass-based material, a nut-based material, a powdered fruitmaterial, a root-based material, a tuber-based material, and avegetable-based material; said density improving textural supplement isselected from the group consisting of extracted arrowroot starch,extracted corn starch, extracted lentil starch, extracted potato starch,and extracted tapioca starch; said moisture improving texturalsupplement is selected from the group consisting of almonds, brazilnuts, cacao, cashews, chestnuts, coconut, filberts, hazelnuts, Indiannuts, macadamia nuts, nut butter, nut oil, nut powder, peanuts, pecans,pili nuts, pine nuts, pinon nuts, pistachios, soy nuts, sunflower seeds,tiger nuts, and walnuts.
 55. The composition according to claim 50,further comprising one or more enhancers, wherein said enhancer isselected from the group consisting of niacin, taurine, glucuronic acid,malic acid, N-acetyl L tyrosine, L-phenylalanine, caffeine, citicoline,and psilocybin.
 56. The composition according to claim 50, wherein: saidinsects are selected from the group consisting of ground insects, insectpowder, whole insects, fermented insects, and spray-dried insects; orsaid insect lipid is selected from the group consisting of palmitoleicacid, linoleic acid, alpha-linoleic acid, oleic acid, gamma-linoleicacid, and stearic acid.
 57. The composition according to claim 50,wherein the composition comprises an extrudate.
 58. The compositionaccording to claim 50, further comprising one or more biocatalyst,wherein said biocatalyst is selected from the group consisting of yeast,bacteria, and a fungus.
 59. The composition according to claim 50,further comprising one or more flavorings, wherein said flavoring isselected from the group consisting of allspice berries, anise seed,annato seed, basil, bay leaves, black pepper, buttermilk, caraway,cayenne, celery seed, cheese culture, chervil, chile powder, chives,cilantro, cinnamon, cloves, coriander, cream of tartar, cubeb berries,cumin, curry, dextrose, dill, fennel, fenugreek, file powder, garlicpowder, ginger, grapefruit peel, green peppercorns, horseradish powder,juniper berries, lavender, lemon grass powder, lemon peel, lime peel,long pepper, marjoram, molasses, mustard, natural smoke flavor, nigellaseeds, nutmeg, onion powder, orange peel, oregano, paprika, parsley,poppy seed, powdered cheese, red pepper, rose petals, rosemary, saffron,sage, star anise, sugar maple, sumac, tamarind, tangerine peel,tarragon, thyme, tomatillo powder, tomato powder, turmeric, vanillaextract, wasabi powder, whey, and white peppercorns.
 60. The compositionaccording to claim 50, wherein said water is derived from one or morewater treatment processes wherein said water treatment process isselected from the group of cation exchange, anion exchange, membranefiltration, and adsorbent filtration.
 61. A dehydrated food compositionincluding: a mixture comprising water, a distilled biosyntheticcannabinoid derived from a genetically modified microorganism or adistilled non-biosynthetic cannabinoid derived from cannabis plants, andtwo or more ingredients selected from the group consisting of insects, abinding agent, and an acid; wherein: said insects are selected from thegroup consisting of an insect lipid, Orthoptera order of insects,crickets, katydids, weta, lubber, acrida, locusts, cicadas, Hermetiaillucens, beetles, mealworms, yellow mealworm beetles, and Tenebriomolitor; said binding agent is selected from the group consisting ofagar, agave, alginin, arrowroot, carrageenan, collagen, cornstarch, eggwhites, furcellaran, gelatin, guar gum, honey, katakuri starch, locustbean gum, pectin, potato starch, protein, psyllium husks, sago, sugar,syrup, tapioca, vegetable gum, and xanthan gum; said acid is selectedfrom the group consisting of acetic acid, ascorbic acid, benzoic acid,citric acid, formic acid, fumaric acid, hydrochloric acid, lactic acid,malic acid, nitric acid, phosphoric acid, propionic acid, salicylicacid, sulfuric acid, and tartaric acid.
 62. The composition according toclaim 61, wherein the biosynthetic cannabinoid derived from agenetically modified microorganism or the non-biosynthetic cannabinoidderived from cannabis plants is selected from the group consisting ofpowder and a crystal.
 63. The composition according to claim 61, whereinthe composition comprises an extrudate.
 64. The composition according toclaim 61, further comprising one or more oils, wherein said oil isselected from the group consisting of almond oil, an animal-based oil,apricot kernel oil, avocado oil, brazil nut oil, butter, canola oil,cashew oil, cocoa butter, coconut oil, corn oil, cottonseed oil, fishoil, grapeseed oil, hazelnut oil, insect oil, lard, lard oil, macadamianut oil, mustard oil, olive oil, palm kernel oil, palm oil, peanut oil,rapeseed oil, rice oil, rice bran oil, safflower oil, semi-refinedsesame oil, semi-refined sunflower oil, sesame oil, soybean oil, tallowof beef, tallow of mutton, vegetable oil, and walnut oil.
 65. Thecomposition according to claim 61, wherein said water is derived fromone or more water treatment processes wherein said water treatmentprocess is selected from the group of cation exchange, anion exchange,membrane filtration, and adsorbent filtration.
 66. The compositionaccording to claim 61, further comprising one or more enhancers, whereinsaid enhancer is selected from the group consisting of niacin, taurine,glucuronic acid, malic acid, N-acetyl L tyrosine, L-phenylalanine,caffeine, citicoline, and psilocybin.
 67. An extruded and cooked candyfoodstuff composition, wherein the composition is cooked in one or moreselected from the group consisting of a dryer, a dehydrator, and afreeze dryer, the composition includes: a mixture comprising water, adistilled biosynthetic cannabinoid derived from a genetically modifiedmicroorganism or a distilled non-biosynthetic cannabinoid derived fromcannabis plants, and two or more ingredients selected from the groupconsisting of insects, a binding agent, an oil, and an acid; wherein:said insects are selected from the group consisting of an insect lipid,Orthoptera order of insects, crickets, katydids, weta, lubber, acrida,locusts, cicadas, Hermetia illucens, beetles, mealworms, yellow mealwormbeetles, and Tenebrio molitor; said binding agent is selected from thegroup consisting of agar, agave, alginin, arrowroot, carrageenan,collagen, cornstarch, egg whites, furcellaran, gelatin, guar gum, honey,katakuri starch, locust bean gum, pectin, potato starch, protein,psyllium husks, sago, sugar, syrup, tapioca, vegetable gum, and xanthangum; said oil is selected from the group consisting of almond oil, ananimal-based oil, apricot kernel oil, avocado oil, brazil nut oil,butter, canola oil, cashew oil, cocoa butter, cooking oil, corn oil,cottonseed oil, fish oil, grapeseed oil, hazelnut oil, insect oil, lard,lard oil, macadamia nut oil, mustard oil, olive oil, palm kernel oil,palm oil, peanut oil, rapeseed oil, rice oil, rice bran oil, saffloweroil, semi-refined sesame oil, semi-refined sunflower oil, sesame oil,soybean oil, tallow of beef, tallow of mutton, vegetable oil, and walnutoil; said acid is selected from the group consisting of acetic acid,ascorbic acid, benzoic acid, citric acid, formic acid, fumaric acid,hydrochloric acid, lactic acid, malic acid, nitric acid, phosphoricacid, propionic acid, salicylic acid, sulfuric acid, and tartaric acid.68. The composition according to claim 67, wherein the biosyntheticcannabinoid derived from a genetically modified microorganism or thenon-biosynthetic cannabinoid derived from cannabis plants is selectedfrom the group consisting of powder and a crystal.
 69. An extruded andcooked food composition, wherein the composition is cooked in one ormore selected from the group consisting of an oven, a dryer, adehydrator, and a freeze dryer, the composition includes: a mixturecomprising water, a distilled biosynthetic cannabinoid derived from agenetically modified microorganism or a distilled non-biosyntheticcannabinoid derived from cannabis plants, and three or more ingredientsselected from the group consisting of insects, a binding agent, an oil,and an acid; wherein: said insects are selected from the groupconsisting of an insect lipid, Orthoptera order of insects, crickets,katydids, weta, lubber, acrida, locusts, cicadas, Hermetia illucens,beetles, mealworms, yellow mealworm beetles, and Tenebrio molitor; saidbinding agent is selected from the group consisting of agar, agave,alginin, arrowroot, carrageenan, collagen, cornstarch, egg whites,furcellaran, gelatin, guar gum, honey, katakuri starch, locust bean gum,pectin, potato starch, protein, psyllium husks, sago, sugar, syrup,tapioca, vegetable gum, and xanthan gum; said oil is selected from thegroup consisting of almond oil, an animal-based oil, apricot kernel oil,avocado oil, brazil nut oil, butter, canola oil, cashew oil, cocoabutter, cooking oil, corn oil, cottonseed oil, fish oil, grapeseed oil,hazelnut oil, insect oil, lard, lard oil, macadamia nut oil, mustardoil, olive oil, palm kernel oil, palm oil, peanut oil, rapeseed oil,rice oil, rice bran oil, safflower oil, semi-refined sesame oil,semi-refined sunflower oil, sesame oil, soybean oil, tallow of beef,tallow of mutton, vegetable oil, and walnut oil; said acid is selectedfrom the group consisting of acetic acid, ascorbic acid, benzoic acid,citric acid, formic acid, fumaric acid, hydrochloric acid, lactic acid,malic acid, nitric acid, phosphoric acid, propionic acid, salicylicacid, sulfuric acid, and tartaric acid.
 70. The composition according toclaim 69, wherein the biosynthetic cannabinoid derived from agenetically modified microorganism or the non-biosynthetic cannabinoidderived from cannabis plants is selected from the group consisting ofpowder and a crystal.
 71. The composition according to claim 69, furthercomprising a binding agent mass ratio ranging from between 10 to 750pounds of the binding agent per ton of the composition.
 72. Thecomposition according to claim 69, further comprising one or moreflavorings, wherein said flavoring is selected from the group consistingof allspice berries, anise seed, annato seed, basil, bay leaves, blackpepper, buttermilk, caraway, cayenne, celery seed, cheese culture,chervil, chile powder, chives, cilantro, cinnamon, cloves, coriander,cream of tartar, cubeb berries, cumin, curry, dextrose, dill, fennel,fenugreek, file powder, garlic powder, ginger, grapefruit peel, greenpeppercorns, horseradish powder, juniper berries, lavender, lemon grasspowder, lemon peel, lime peel, long pepper, marjoram, molasses, mustard,natural smoke flavor, nigella seeds, nutmeg, onion powder, orange peel,oregano, paprika, parsley, poppy seed, powdered cheese, red pepper, rosepetals, rosemary, saffron, sage, star anise, sugar maple, sumac,tamarind, tangerine peel, tarragon, thyme, tomatillo powder, tomatopowder, turmeric, vanilla extract, wasabi powder, whey, and whitepeppercorns.
 73. The composition according to claim 69, wherein saidwater is derived from one or more water treatment processes wherein saidwater treatment process is selected from the group of cation exchange,anion exchange, membrane filtration, and adsorbent filtration.
 74. Thecomposition according to claim 69, further comprising one or moreenhancers, wherein said enhancer is selected from the group consistingof niacin, taurine, glucuronic acid, malic acid, N-acetyl L tyrosine,L-phenylalanine, caffeine, citicoline, and psilocybin.